for restricted circulation onlyforestsclearance.nic.in/writereaddata/forma/... · 2018. 6. 20. ·...

Indian Oil Corporation Limited (Pipelines Division)

November 2015

For Restricted Circulation Only

Asansol

Haldia

Barauni

Jasidih

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DFR ndash Haldia-Barauni Product Pipeline of 40

Contents

Chapter No

Description Page No

Executive Summary [i] - [xi]

I Introduction 2

II Need and Justification 4

III Design Philosophy 10

IV Project Description 11

V Safety Health amp Environment 25

VI Capital Costs 31

VII Operating Costs 34

VIII Financial Analysis 36

IX Conclusions amp Recommendations 38

Annexures

A Hydraulic Gradient Annexure-I

B System Configuration Annexure-II

C Indicative Route Annexure-III

D Completion Schedule Annexure-IV

E Capital Cost Annexure-V

F Operating Cost Annexure-VI

Appendix-i (Highlights of Geophysical Survey)

Appendix-ii (Optimization Study Report)

EXECUTIVE SUMMARY

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Executive Summary ndash Haldia-Barauni Product Pipeline [i]

EXECUTIVE SUMMARY

10 INTRODUCTION

11 IOC has presently three petroleum product pipelines in Eastern region viz Haldia-Barauni Pipeline (HBPL) Barauni-Kanpur Pipeline (BKPL) and Haldia-Mourigram-Rajbandh Pipeline (HMRPL) for supply of petroleum products in the states of WestBengal UP Bihar and Jharkhand HBPL is delivering petroleum products to MarketingTerminals at Rajbandh Jasidih and to Barauni for onward transportation of productsthrough BKPL from Barauni to Marketing Terminals at Patna Mughalsarai AllahabadKanpur and Lucknow

12 The existing 526 km long HBPL was laid in 1967 and is in operation for more than48 years This pipeline has a history of external as well as internal corrosion and leaksfailures have occurred in the past Presently the pipeline is being operated at deratedpressure due to these reasons

13 Pipeline section of HBPL (from chainage 220 km to chainage 261 km) around Asansolarea falls in the coal belt area This section of the HBPL has long history of itscloseness to several coal fire zones soil subsidence which may lead to in-servicefailure of the pipeline

14 Recent geographical survey by NIRM (National Institute of Rock Mechanics) indicatesthat zone of subsidence is approaching below our pipeline The Eastern Coal Fieldauthorities are also constantly pursuing IOC for shifting HBPL from coal belt area inAsansol region stating that significant quantity of coal is blocked under our pipeline

15 A reconnaissance survey was carried out to identify alternative routes for bypassing re-routing the pipeline section of HBPL falling in Asansol coal belt area The length ofthese routes varies from about 88 km to 143 km

16 The actual throughput of the pipeline was 121 MMTPA for 2014-15 which is almostequal to the design capacity of 125 MMTPA of pipeline Thus the pipeline is almostsaturated presently as per design capacity

17 As per Optimization study report dated 2072015 the existing capacity of HBPL willnot be sufficient to meet the demand of petroleum products sourced from HaldiarefineryHaldia coastal input to Marketing Terminals at Jasidih Patna MughalsaraiAllahabad Kanpur Lucknow Motihari and Baitalpur in 2018-19 The throughputrequirement of HBPL will vary from 21 MMTPA in 2018-19 to 40 MMTPA in2021-22 for different scenarios to meet the demand of above mentioned MarketingTerminals

18 Therefore from above it is imperative that laying of new product pipeline from Haldiato Barauni is the most suitable alternative from safety as well as long-term requirement




EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION











Executive Summary ndash Haldia-Barauni Product Pipeline [ii]

point of view Further this pipeline would act as a critical link for cost-effectivetransportation of IOC products which would be sourced from HaldiaCoastal input toMarketing Terminals in West Bengal UP Bihar and Jharkhand

19 Accordingly Detailed Feasibility Report (DFR) has been prepared for laying a newproduct pipeline from Haldia to Barauni via Jasidih This DFR broadly deals with theneed and justification system configuration cost technical viability implementationmethodology financial analysis and other details of the proposal involving laying of 18inch diameter 535 km long Haldia-Barauni Product Pipeline from Haldia to Baraunifor delivering petroleum products to Marketing Terminals at Jasidih amp Barauni and foronward transportation of products through the existing BKPL

20 NEED AND JUSTIFICATION

21 Existing HBPL was commissioned in the year 1967 with API 5L-X46 grade pipesmanufactured by low frequency Electric Resistance Welding (ERW) process Thepipeline is in operation for more than 48 years and internalexternal corrosion of thepipeline coupled with fatigue induced by pressure cycles during operation has made thispipeline vulnerable to failures

22 The existing pipeline is being operated at derated pressure of 63 kgcm2 between Haldiaand Asansol Pump Station and 45 kgcm2 between Asansol and Barauni since earlyeighties whereas Maximum Allowable Operating Pressure (MAOP) of pipeline is82 kgcm2 as per design

23 Internal corrosion has been an issue in this pipeline since commissioning and the initial20 km of this pipeline from Haldia which was severely affected with internalcorrosion was replaced in 1986

24 The report on Intelligent Pig Survey carried out in 2010 has also indicated more thanaverage internal corrosion anomalies in this pipeline (except for the initial 20 km linewhich was replaced in 1986)

25 In order to have a realistic assessment of soil condition of RoW in the coal belt areaMs National Institute of Rock Mechanics (NIRM) is being engaged periodically andthey have undertaken geophysical survey in the year 2008 2013 and latest in January2015 In the earlier two geophysical surveys potential threat zones where chances ofsubsidence or presence of cavity pockets were suspected in shallow subsurfaceproximate to this pipeline section were backfilled to avoid any possible threat likecaving in of the surface As per latest survey carried out in January 2015 it wasobserved that a large area below pipeline is having cavity or weak zone within 5-10 mdepth which is potentially dangerous and might trigger a wide-spread subsidence in thearea thereby threatening the stability of the pipeline

























Executive Summary ndash Haldia-Barauni Product Pipeline [iii]

26 Based on the reconnaissance survey three routes were suggested between Ch 170 kmto 289 km for bypassing re-routing the HBPL pipeline section falling in Asansol coalbelt area The length of these routes varies from about 88 km to 143 km

27 However even after re- routing of existing pipeline section of HBPL which is passingthrough the coal belt area around Asansol there will not be any increase in throughputas the pressure of pipeline sections upstream and downstream of this pipeline sectionwould be restricted to the derated pressure and to meet the demand of the consumptioncenters fed through HBPL a new pipeline would also be required Accordingly a newpipeline is proposed from Haldia to Barauni which will not only ensure fulfilment ofenhanced throughput requirement which is required in next 5 years but would alsoeliminate the probability of subsidence and in-service failure of the pipeline

28 Presently the coastal input at Haldia is limited to 084 MMTPA due to Haldia Jettyrestrictions Therefore sourcing of the additional requirement of products on long-termbasis from Paradip refinery through laying of another pipeline from Paradip to Haldiaie Paradip-Somnathpur-Haldia pipeline (PSHPL) and linking with the proposed HBPLis being examined by Corporate Optimization

29 The actual throughput of HBPL for last three years is as under

Fig in MMTPA

210 As seen from above actual throughput of the pipeline in the recent time has been closeto the design capacity of the pipeline ie 125 MMTPA

211 As per the Optimization report dated 2072015 the projected throughput of HBPLvaries from 21 MMTPA in 2018-19 to 40 MMTPA in 2021-22 for different scenariosBrief of Optimization report findings for the most optimumfeasible scenarios alongwith assumptions are as under

Assumptions

Both PSHPL and Mathura-Tundla pipeline (MTPL) extension to Gwaria (Kanpur ampLucknow) are operational in 2021-22

Findings

i) HBPL throughput requirement is 21 MMTPA However the pipeline will getsaturated before 2018-19 with existing HBPL capacity even after considering themaximum achievable capacity of 17 MMTPA Projected saving is Rs5525croreyear for the incremental throughput

ii) The throughput requirement in 2021-22 is 40 MMTPA Projected saving isRs1925 croreyear for the incremental throughput

Year Actual Throughput

2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121



Executive Summary ndash Haldia-Barauni Product Pipeline [iv]

212 Section-wise throughput is as under

Pipeline Section Throughput (MMTPA)

2018-19 2021-22Haldia- Jasidih 21 40Jasidih-Barauni 16 35

2121 From above it is evident that the saving of Rs1925 croreyear can be accrued from theproposed pipeline for throughput of 40 MMTPA

213 The saving of the proposed HBPL in 2018-19 and 2021-22 is mainly due to reductionof coastal input at Haldia to Nil from present level of 084 MMTPA and reduction inrail loading from Paradip and due to supply of product requirement for BKPL ToPs andPatna-Motihari-Baitalpur Branch Pipeline (PMBPL) ToPs through pipeline mode inproject case against rail in the base case and associated changes in transportationlogistics

214 Scenario Analysis of Throughput Optimization

2141 Analysis of various scenarios without PSHPL amp MTPL extension to Gwaria (KanpurLucknow) being operational by 2021-22 has been carried out in Optimization study andthe results indicate that

i) MTPL extension to Gwaria (Kanpur Lucknow) being operational by 2021-22 hasnegligible impact on throughput and savings for the proposed HBPL For the year2021-22 the throughput remains same ie 4 MMTPA however savings is reducedto Rs 170 crore if MTPL extension does not materialize

ii) However without PSHPL being operational by 2021-22 there is significantimpact in throughput and savings for the proposed HBPL For the year 2021-22the throughput is reduced to 23 MMTPA and savings is reduced to onlyRs17 crore

2142 Reconnaissance survey for Paradip-Somnathpur-Haldia Pipeline has already beencompleted and feasibility study is in progress The proposal for Paradip-Somnathpur-Haldia Pipeline will be put up shortly with a target to commission the same by2021-22

2143 It can be seen from the above that the present HBPL system would not be able to pumpthe required throughput of 21 MMTPA and in order to meet the enhanced throughputrequirement and due to constraints associated with the present HBPL system there isan urgent need to lay the proposed Haldia-Barauni pipeline via Jasidih Accordinglythis proposal is being put up for laying a 18 inch diameter 535 km long productpipeline between Haldia and Barauni for meeting short-term as well as long-termthroughput requirements































Executive Summary ndash Haldia-Barauni Product Pipeline [v]

215 Justification for the Proposed Pipeline

2151 HBPL is a critical link for supply of products from ParadipHaldia refinerycoastal inputs atHaldia to demand centres in Bihar UP and Jharkhand Derating of the pipeline andleaksfailures have resulted in restricted capacity of existing pipeline and the present productpositioning arrangement would not be adequate in meeting the future demand in a reliable andcost-effective manner It may be observed that even after considering maximum achievablecapacity the existing HBPL system would not be sufficient to meet the throughputrequirement in short-term (21 MMTPA) as well as in long-term (40 MMTPA) scenarioswhich otherwise would necessitate laying of another pipeline or else would result in un-economic supply of products to BKPL ToPs by rail transportation

2152 Therefore considering the deteriorating health of the existing pipeline request from EasternCoal Field authorities for shifting of pipeline from the coal belt area as well as and foroperational safety of pipeline amp capacity restrictions in existing pipeline for meeting the short-term as well as long-term throughput requirement it is prudent to lay new product pipelinefrom Haldia to Barauni This pipeline will ensure cost-effective transportation anduninterrupted supply of petroleum products of IOC from HaldiaCoastal input in short-termand from Paradip through proposed PSHPL in long-term to Marketing Terminals in UPBihar and Jharkhand thereby maintaining IOC market share capturing new market areas inUP Bihar and West Bengal

2153 With the proposed HBPL IOC would be able to save substantially in product positioning costat aforementioned ToPs which will also avoid multiple handling of products (CoastalRailloadingunloading) resulting into reduction in transit losses

2154 It has been established the world over that pipelines are the superior means for transportationof petroleum products compared to other modes viz rail road tankers etc due to theirinherent advantages like reliability economy safety flexibility low energy consumption lowtransit losses and negligible impact on environment Construction of pipelines also providesrelief to other modes of transportation for movement of essential goods commodities andpassengers and reduces the hazards associated with transportation of petroleum products byroad

2155 In view of the above the proposal of laying a new pipeline from Haldia to Barauni viaexisting Jasidih delivery terminal merits consideration

216 Design Capacity

2161 Based on the Optimization Study considering the maximum corporate savings withmost optimum scenario (ie both PSHPL and MTPL Extn by 2021-22) the projectedthroughput in 2018-19 would be 21 MMTPA and 40 MMTPA in 2021-22

It is proposed to implement pipeline project in 2 stages as under










216 Design Capacity












216 Design Capacity





Executive Summary ndash Haldia-Barauni Product Pipeline [vi]

Stage-I Design capacity of 34 MMTPA with delivery station at Jasidih and withoutany intermediate pumping station

Stage-II Design Capacity of 46 MMTPA with addition of an intermediate pumpingstation at Bolpur

2162 The proposed Stage-I of the project will be implemented first Thus this proposal isbeing prepared for approval of Stage-I only A separate proposal will be put up forStage-II subsequent to the successful commissioning and realization of projectedthroughput as envisaged in Stage-I

30 PROJECT DESCRIPTION

31 Systems Hydraulics

311 Based on the pipeline throughput requirements the pipeline system has been designedfor implementation in 2 stages Hydraulic have been worked out for both the stagesDetails are as under

Stage Design Capacity(MMTPA)

Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation

Stage-I 34 500 Haldia - Jasidih Barauni

Stage-II 46 676 Haldia Bolpur Jasidih Barauni

Line Size MAOP

Pipeline Length Line Size MAOP

(km) OD(inch) WT(inch) Grade mcl Kgcm2

Haldia-Barauni 535 18 025 API 5L-X70 1158 98

312 Hydraulics

Stage-I

S No Station Chainage(km)

Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50



Executive Summary ndash Haldia-Barauni Product Pipeline [vii]

km Kilometre m Metre mcl Metre Column of Liquid (HSD) SDH Station DischargeHead RH Residual Head IPS Intermediate Pump Station MLPUs Main LinePumping Units

Note - In Stage-I Bolpur will be designed considering a scrapper station and the samewill be converted to pump station in Stage-II

32 System Configuration

321 The new pump station will be constructed at newly acquired land (20 acre) nearexisting PHBPL Haldia station and new pipeline will originate from this pump stationThe booster pump station will remain at the existing pumping station (located insideHaldia refinery) However the existing booster pumps will be replaced with highercapacity booster pumps

322 Stage-I configuration of the pipeline system broadly comprises the following

i) Laying of 535 km 18rdquoOD x 025rdquo WT API-5L-X70 Grade pipe from proposedmainline pump station at PHBPL Haldia to the existing terminal station at HBPLBarauni

ii) Replacement of 2 booster pumps (1+1) at existing booster station at HBPL Haldia

iii) Installation of 3 motor-driven MLPUs (2 operating + 1 standby) at new pumpstation at PHBPL Haldia

iv) Laying of about 10 km 18rdquoOD x 0281rdquo WT pipe from existing pump station atHBPL Haldia to proposed new mainline pump station at PHBPL Haldia

v) Scrapper station at Bolpur

vi) Hookup with existing marketing terminal at Jasidih

vii) Total No of Mainline SVs (including River MOVs) envisaged is 41

viii)Station facilities modifications at Barauni to accommodate increased throughputrequirement

ix) Conversion of 1 LBT Tank of 3500 kl capacity at Barauni from HSD to MSservice

323 The facilitiesMLPUs designedprocured for Stage-I will be adequate to meet theconfiguration of both Stage-I amp Stage-II

324 In Stage-II configuration the scrapper station at Bolpur will be converted into pumpingstation by installing 3 motor-driven MLPUs

325 After commissioning of this pipeline the existing intermediate pump station at Asansolwould become redundant and would be de-commissioned Mainline pumping units atAsansol would be suitably utilized at some other pipeline location as per requirement

326 Additional facilities at Haldia refinery will involve engineering and execution of a newcommon 18 inch discharge header for hooking up with the existing booster pumpdischarges from refinery tanks and laying of this pipeline up to HBPL boosters













































Executive Summary ndash Haldia-Barauni Product Pipeline [viii]

327 Additional marketing facilities at Haldia Jasidih will involve modification to existingpipes valves amp flanges etc to accommodate higher flow rate

33 Pipeline Route

331 Pipeline will originate from PHBPL pump station at Haldia The new pipeline would belaid in common RoW of PHBPL up to Bolpur station (ch 206 km) from HaldiaThereafter it will travel in new RoW via Jasidih from ch 206 km to ch 465 kmSubsequently from ch 465 km to ch 535 km the pipeline will follow the existing RoWof PHBPL Existing HBPLHMRBPL pump station is in the Haldia refinery premiseswhich is about 10 km away from PHBPL Haldia pump station The existing commonRoW from HBPL booster station to PHBPL will be used for the proposed 10 kmpipeline and additionally approx 2 km of pipeline would be required in new RoW forhooking up with new station at PHBPL Haldia

34 Operation Philosophy

341 Delivery of products to depots can be through heart-cut or blocked out mode as per therequirement but considering that 85 of total pipeline throughput to be delivered atBarauni the facilities have been designed for blocked out delivery to Barauni Thetypical pumping sequence in the pipeline would be as under

PCKSKOndashHSDndashPCKSKOndashMSndashPCKSKOndashHSDndashPCKSKO

342 The total line fill of the pipeline from Haldia to Barauni would be about 83050 kl

343 Minimum Batch Length and Tankages

3431 Minimum batch length for MS and HSD has been worked out considering simultaneousdelivery at Jasidih and Barauni Considering absorption of 1 SKO in MS and 1SKO in HSD minimum batch length required is 30000 kl and 33000 kl for MS andHSD respectively Considering the small delivery volume at Jasidih interfaceabsorption of entire batch will be done at Barauni Batch length of SKO would dependon its requirement However a minimum PCKSKO plug of 1000 kL would be requiredfor absorption of interface

3432 In case of non-availability of MSHSD batch as above or due to unplanned shutdown ofthe pipeline interface might increase in the pipeline and some unabsorbed interface maybe there which would be delivered in the transmix tanks at Barauni MS-PCKSKOinterface would be received in MS Transmix tank and HSD-PCKSKO interface wouldbe received in HSD transmix tank A part of the interface received in transmix tanksmay be blended online in the products being delivered in tanks at Barauni Remainingpart of the unabsorbed interface if any from transmix tank would be pumped to crudeoil delivery header of PHBPL Barauni for blending in crude oil and further processingby Barauni Refinery Facilities for the same have been considered at Barauni

35 Implementation Methodology

351 It is proposed to take up execution of the project through in-house expertise





33 Pipeline Route















33 Pipeline Route













Executive Summary ndash Haldia-Barauni Product Pipeline [ix]

36 Statutory Clearances

361 Suitable actions will be taken for obtaining all relevant statutory clearances for theproject from concerned authorities as applicable

37 Construction Schedule

371 The proposed scheme is expected to be completed in a period of about 36 months afterreceipt of all statutory clearances

38 Manpower Requirement

381 The manpower requirement would be about 67 during construction phase excludingLine Patrolmen (LPM) The requirement of manpower is expected to be met throughinternal deployment as well as by induction of competent personnel The requirement ofLPM for the new RoW is envisaged to be outsourced

382 The existing manpower at Haldia Jasidih and Barauni would be adequate to handle theoperating phase and manpower presently stationed at Asansol would be suitablyre-deployed

40 CAPITAL COST

41 The pipeline system from Haldia to Barauni is estimated to cost Rs1038 croreincluding a foreign exchange component of Rs8 crore at November 2015 price levelThis comprises Rs1021 crore towards cost of the pipeline system Rs11 crore towardsmodification to existing piping valves etc at the existing Haldia and Jasidih MarketingTerminal and Rs6 crore towards modification to existing pipes valves amp fittings etc atHaldia refinery

50 OPERATING COST

51 Operating cost of the pipeline system includes the incremental cost of powerfuel formainline pumping units utilities consumables and full repair and maintenance for theproposed pipeline etc

52 The incremental operating cost of Haldia-Barauni pipeline for Stage-I is estimated to beabout Rs19 crore at November 2015 price level

60 CONDEMNATION

61 The existing 1275OD pipeline would continue to remain in use till completion ofproposed scheme

62 Upon successful commissioning of new pipeline action would be initiated forcondemnation of existing pipeline











40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION





Executive Summary ndash Haldia-Barauni Product Pipeline [x]

63 The existing intermediate pumping station at Asansol would be redundant and would bedecommissioned Mainline pumping units at Haldia amp Asansol would be suitablyutilized at some other pipeline location as per requirement

70 FINANCIAL ANALYSIS

71 Capital cost of the project is considered to be financed through internalresourcescommercial borrowings For the purpose of financial analysis debtequityratio of 11 has been considered with interest at the rate of 940 per annum on debtand repayment in 8 equal annual instalments with one-year moratorium period from thedate of commissioning Requirement of working capital will be met through internalresources

72 Financial analysis for the proposal has been carried out taking into account thefollowing

i) Incremental throughput and corporate saving

ii) Capital cost of the pipeline and its operation for 25 years

iii) Throughput as indicated in the optimization study for 2018-19 and 2021-22

iv) Corporate savings assessed in the optimization study as revenue

v) Benefit due to lower transit loss in pipeline transportation compared to typicallosses permitted for transportation through other modes of transportation

vi) Savings in loadingunloading charges

73 Results of the financial analysis are as under

IRR [ROI ()] IRR [ROE ()]

144 167

74 Sensitivity Analysis

741 Results of sensitivity analysis are as underCase IRR [ROI ()] IRR [ROE ()]

Increase in capital cost by 10 133 151Increase in operating cost by 10 142 164Decrease in throughput by 10 131 148All of the above together 119 131

75 From the above it can be seen that the calculated IRR is higherequal to the currenthurdle rate of 12 (for pipeline projects) in all scenarios and the project is financiallyviable

80 CONCLUSIONS AND RECOMMENDATIONS

81 The products from Haldia refinery coastally received are transported through HBPL tothe demand centers in W Bengal and Jharkhand and also Barauni for further movementthrough BKPL for the ToPs in Bihar and UP
















144 167






















144 167









Executive Summary ndash Haldia-Barauni Product Pipeline [xi]

82 The existing HBPL is in operation for more than 48 years and during this period itshealth condition has been deteriorated significantly The pipeline has history ofleaksfailures Presently the pipeline is being operated at derated pressure due to thesereasons

83 However even after re- routing of existing pipeline section of HBPL which is passingthrough the coal belt area around Asansol there will not be any increase in throughputas the pressure of pipeline sections upstream and downstream of this pipeline sectionwould be restricted to the derated pressure and to meet the demand of the consumptioncenters fed through HBPL a new pipeline would also be required

84 Accordingly a new pipeline is proposed from Haldia to Barauni which will not onlyensure meeting the enhanced throughput requirement which is required in next 5 yearsbut would also eliminate the probability of subsidence and in-service failure of thepipeline

85 HBPL is a critical link for supply of products from ParadipHaldia refinerycoastalinputs at Haldia to demand centres in Bihar UP and Jharkhand Derating of thepipeline and leaksfailures have resulted in restricted capacity of existing pipeline andthe present product positioning arrangement would not be adequate in meeting thefuture demand in a reliable and cost-effective manner It may be observed that evenafter considering maximum achievable capacity the existing HBPL system would notbe sufficient to meet the throughput requirement in short-term (21 MMTPA) as well aslong-term (40 MMTPA) scenarios which otherwise would necessitate laying ofanother pipeline or else would result in un-economic supply of products to BKPL ToPsby rail transportation

86 Therefore considering the deteriorating health of the existing pipeline request fromEastern Coal Field authorities for shifting of pipeline from the coal belt area as well asfor operational safety of pipeline amp capacity restrictions in existing pipeline formeeting the short-term as well as long-term throughput requirement it is prudent to laynew product pipeline from Haldia to Barauni This pipeline will ensure cost-effectivetransportation and uninterrupted supply of petroleum products of IOC fromHaldiaCoastal input in short-term and from Paradip through proposed PSHPL inlong-term to Marketing Terminals in UP Bihar and Jharkhand thereby maintainingIOC market share capturing new market areas in UP Bihar and West Bengal

87 In view of the inherent advantages of pipeline transportation as discussed above and theestimated economic benefits it is recommended to lay a new Haldia-Barauni productpipeline at an estimated cost of Rs1038 crore including a foreign exchange componentof Rs8 crore at November 2015 price level This comprises Rs1021 crore towards costof the pipeline system Rs11 crore towards modification to existing piping valves etcat the existing Haldia and Jasidih Marketing Terminal and Rs6 crore towardsmodification to existing pipes valves amp fittings etc at Haldia refinery

-- --










-- --










-- --

INTRODUCTION



DFR ndash Haldia-Barauni Product Pipeline Page 2 of 40

CHAPTER - I

10 INTRODUCTION

11 IOC has presently three petroleum product pipelines in Eastern region viz Haldia-

Barauni Pipeline (HBPL) Barauni-Kanpur Pipeline (BKPL) and Haldia-Mourigram-

Rajbandh Pipeline (HMRPL) for supply of petroleum products in the states of West

Bengal UP Bihar and Jharkhand HBPL is delivering petroleum products to

Marketing Terminals at Rajbandh Jasidih and to Barauni for onward transportation of

products through BKPL from Barauni to Marketing Terminals at Patna Mughalsarai

Allahabad Kanpur and Lucknow

12 The existing 526 km long HBPL was laid in 1967 and is in operation for more than

48 years This pipeline has a history of external as well as internal corrosion and

leaks failures have occurred in the past Presently the pipeline is being operated at

derated pressure due to these reasons

13 Pipeline section of HBPL (from chainage 220 km to chainage 261 km) around

Asansol area falls in the coal belt area This section of the HBPL has long history of

its closeness to several coal fire zones soil subsidence which may lead to in-service

failure of the pipeline

14 Recent geographical survey by NIRM (National Institute of Rock Mechanics)

indicates that zone of subsidence is approaching below our pipeline The Eastern Coal

Field authorities are also constantly pursuing IOC for shifting HBPL from coal belt

area in Asansol region stating that significant quantity of coal is blocked under our

pipeline

15 A reconnaissance survey was carried out to identify alternative routes for bypassing

re-routing the pipeline section of HBPL falling in Asansol coal belt area The length

of these routes varies from about 88 km to 143 km

16 The actual throughput of the pipeline was 121 MMTPA for 2014-15 which is almost

equal to the design capacity of 125 MMTPA of pipeline Thus the pipeline is almost

saturated presently as per design capacity




17 As per Optimization study report dated 2072015 the existing capacity of HBPL will

not be sufficient to meet the demand of petroleum products sourced from Haldia

refineryHaldia coastal input to Marketing Terminals at Jasidih Patna Mughalsarai

Allahabad Kanpur Lucknow Motihari and Baitalpur in 2018-19 The throughput

requirement of HBPL will vary from 21 MMTPA in 2018-19 to 40 MMTPA in

2021-22 for different scenarios to meet the demand of above mentioned Marketing

Terminals

18 Therefore from above it is imperative that laying of new product pipeline from

Haldia to Barauni is the most suitable alternative from safety as well as long-term

requirement point of view Further this pipeline would act as a critical link for cost-

effective transportation of IOC products which would be sourced from

HaldiaCoastal input to Marketing Terminals in West Bengal UP Bihar and

Jharkhand

19 Accordingly Detailed Feasibility Report (DFR) has been prepared for laying a new

product pipeline from Haldia to Barauni via Jasidih This DFR broadly deals with the

need and justification system configuration cost technical viability implementation

methodology financial analysis and other details of the proposal involving laying of

18 inch diameter 535 km long Haldia-Barauni Product Pipeline from Haldia to

Barauni for delivering petroleum products to Marketing Terminals at Jasidih amp

Barauni and for onward transportation of products through the existing BKPL

NEED AND JUSTIFICATION




CHAPTER ndash II


21 Existing HBPL was commissioned in the year 1967 with API 5L-X46 grade pipes

manufactured by low frequency Electric Resistance Welding (ERW) process The

pipeline is in operation for more than 48 years and internalexternal corrosion of the

pipeline coupled with fatigue induced by pressure cycles during operation has made

this pipeline vulnerable to failures

22 The existing pipeline is being operated at derated pressure of 63 kgcm2 between

Haldia and Asansol Pump Station and 45 kgcm2 between Asansol and Barauni since

early eighties whereas Maximum Allowable Operating Pressure (MAOP) of pipeline

is 82 kgcm2 as per design

23 Internal corrosion has been an issue in this pipeline since commissioning and the

initial 20 km of this pipeline from Haldia which was severely affected with internal

corrosion was replaced in 1986

24 The report on Intelligent Pig Survey carried out in 2010 has also indicated more than

average internal corrosion anomalies in this pipeline (except for the initial 20 km line

which was replaced in 1986)

25 In order to have a realistic assessment of soil condition of RoW in the coal belt area

Ms National Institute of Rock Mechanics (NIRM) is being engaged periodically and

they have undertaken geophysical survey in the year 2008 2013 and latest in January

2015 In the earlier two geophysical surveys potential threat zones where chances of

subsidence or presence of cavity pockets were suspected in shallow subsurface

proximate to this pipeline section were backfilled to avoid any possible threat like

caving in of the surface As per latest survey carried out in January 2015 it was

observed that a large area below pipeline is having cavity or weak zone within 5-10 m

depth which is potentially dangerous and might trigger a wide-spread subsidence in

the area thereby threatening the stability of the pipeline




26 Based on the reconnaissance survey three routes were suggested between Ch 170 km

to 289 km for bypassing re-routing the HBPL pipeline section falling in Asansol coal

belt area The length of these routes varies from about 88 km to 143 km

27 However even after re- routing of existing pipeline section of HBPL which is

passing through the coal belt area around Asansol there will not be any increase in

throughput as the pressure of pipeline sections upstream and downstream of this

pipeline section would be restricted to the derated pressure and to meet the demand of

the consumption centers fed through HBPL a new pipeline would also be required

Accordingly a new pipeline is proposed from Haldia to Barauni which will not only

ensure fulfilment of enhanced throughput requirement which is required in next 5

years but would also eliminate the probability of subsidence and in-service failure of

the pipeline

21 Presently the coastal input at Haldia is limited to 084 MMTPA due to Haldia Jetty

restrictions Therefore sourcing of the additional requirement of products on long-

term basis from Paradip refinery through laying of another pipeline from Paradip to

Haldia ie Paradip-Somnathpur-Haldia pipeline (PSHPL) and linking with the

proposed HBPL is being examined by Corporate Optimization


Fig in MMTPA

221 As seen from above actual throughput of the pipeline in the recent time has been

close to the design capacity of the pipeline ie 125 MMTPA

23 As per the Optimization report dated 2072015 the projected throughput of HBPL

varies from 21 MMTPA in 2018-19 to 40 MMTPA in 2021-22 for different

scenarios Brief of Optimization report findings for the most optimumfeasible

scenarios along with assumptions are as under


2012-13 125 2013-14 101 2014-15 121




Assumptions

Both PSHPL and Mathura-Tundla pipeline (MTPL) extension to Gwaria (Kanpur amp

Lucknow) are operational in 2021-22

Findings

i) HBPL throughput requirement of 21 MMTPA will get saturated before

2018-19 with existing HBPL capacity even after considering the maximum

achievable capacity of 17 MMTPA Projected saving is Rs5525 croreyear for

the incremental throughput

ii) The throughput requirement in 2021-22 is 40 MMTPA Projected saving is

Rs1925 croreyear for the incremental throughput

24 Section-wise throughput

241 Section-wise amp product-wise throughput is given as under

Pipeline Section Throughput (TMT)

2018-19 2021-22

HSD MS SKO TOTAL HSD MS SKO TOTAL

Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440

Product handling at Haldia (RailCoastal)

By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0

242 From above it is evident that the saving of Rs1925 croreyear can be accrued from

the proposed pipeline for throughput of 40 MMTPA

25 The saving of the proposed HBPL in 2018-19 and 2021-22 is mainly due to reduction

of coastal input at Haldia to Nil from present level of 084 MMTPA and reduction in

rail loading from Paradip and due to supply of product requirement for BKPL ToPs

and Patna-Motihari-Baitalpur Branch Pipeline (PMBPL) ToPs through pipeline mode

in project case against rail in the base case and associated changes in transportation

logistics




26 Analysis of Throughput Optimisation

261 Analysis of various scenarios without PSHPL amp MTPL extension to Gwaria (Kanpur

Lucknow) being operational by 2021-22 has been carried out in Optimization study

and the results indicate that

i) MTPL extension to Gwaria (Kanpur Lucknow) being operational by 2021-22

has negligible impact on throughput and savings for the proposed HBPL For

the year 2021-22 the throughput remains same ie 4 MMTPA however savings

is reduced to Rs170 crore if MTPL extension does not materialize

ii) However without PSHPL being operational by 2021-22 there is significant

impact in throughput and savings for the proposed HBPL For the year 2021-22

the throughput is reduced to 23 MMTPA and savings is reduced to only

Rs17 crore

262 Reconnaissance survey for Paradip-Somnathpur-Haldia Pipeline has already been

completed and feasibility study is in progress The proposal for Paradip-Somnathpur-

Haldia Pipeline will be put up shortly with a target to commission the same by

2021-22

263 It can be seen from the above that the present HBPL system would not be able to

pump the required throughput of 21 MMTPA and in order to meet the enhanced

throughput requirement and due to constraints associated with the present HBPL

system there is an urgent need to lay the proposed Haldia-Barauni pipeline via

Jasidih Accordingly this proposal is being put up for laying a 18 inch diameter

535 km long product pipeline between Haldia and Barauni for meeting short-term as

well as long-term throughput requirements


271 HBPL is a critical link for supply of products from ParadipHaldia refinerycoastal

inputs at Haldia to demand centres in Bihar UP and Jharkhand Derating of the

pipeline and leaksfailures have resulted in restricted capacity of existing pipeline and

the present product positioning arrangement would not be adequate in meeting the




future demand in a reliable and cost-effective manner It may be observed that even

after considering maximum achievable capacity the existing HBPL system would not

be sufficient to meet the throughput requirement in short-term (21 MMTPA) as well

as in long-term (40 MMTPA) scenarios which otherwise would necessitate laying of

another pipeline or else would result in un-economic supply of products to BKPL

ToPs by rail transportation

272 Therefore considering the deteriorating health of the existing pipeline request from

Eastern Coal Field authorities for shifting of pipeline from the coal belt area as well as

and for operational safety of pipeline amp capacity restrictions in existing pipeline for

meeting the short-term as well as long-term throughput requirement it is prudent to

lay new product pipeline from Haldia to Barauni This pipeline will ensure cost-

effective transportation and uninterrupted supply of petroleum products of IOC from

HaldiaCoastal input in short-term and from Paradip through proposed PSHPL in

long-term to Marketing Terminals in UP Bihar and Jharkhand thereby maintaining

IOC market share capturing new market areas in UP Bihar and West Bengal

273 With the proposed HBPL IOC would be able to save substantially in product

positioning cost at aforementioned ToPs which will also avoid multiple handling of

products (CoastalRail loadingunloading) resulting into reduction in transit losses

274 It has been established the world over that pipelines are the superior means for

transportation of petroleum products compared to other modes viz rail road tankers

etc due to their inherent advantages like reliability economy safety flexibility low

energy consumption low transit losses and negligible impact on environment

Construction of pipelines also provides relief to other modes of transportation for

movement of essential goods commodities and passengers and reduces the hazards

associated with transportation of petroleum products by road

275 In view of the above the proposal of laying a new pipeline from Haldia to Barauni via

existing Jasidih delivery terminal merits consideration

276 Study report received from CO (Optimization) is enclosed as Appendix-ii




28 Design Capacity

281 Based on the Optimization Study considering the maximum corporate savings with

most optimum scenario (ie both PSHPL and MTPL Extn by 2021-22) the projected

throughput in 2018-19 would be 21 MMTPA and 40 MMTPA in 2021-22


Stage-I Design capacity of 34 MMTPA with delivery station at Jasidih and

without any intermediate pumping station

Stage-II Design Capacity of 46 MMTPA with addition of an intermediate

pumping station at Bolpur

282 The proposed Stage-I of the project will be implemented first Thus this proposal is

being prepared for approval of Stage-I only A separate proposal will be put up for

Stage-II subsequent to the successful commissioning and realization of projected

throughput as envisaged in Stage-I

DESIGN PHILOSOPHY




CHAPTER - III

30 DESIGN PHILOSOPHY

31 Introduction

311 This chapter covers the basic data and design parameters adopted for preparing this

report

32 Products For Transportation

321 The proposed Haldia-Barauni pipeline system is envisaged to be used for

transportation of HSD MS SKO and ATF

33 Product Characteristics

331 The pipeline system has been designed on the basis of HSD having the following

characteristics

Specific Gravity 085

Kinematic Viscosity 5 cst

34 Design Parameters

341 The system has been designed based on 8000 hours of operation in a year

342 Maximum allowable operating pressure (MAOP) of the system is based on 72 of

the specified minimum yield strength of the pipe material

343 No corrosion allowance has been considered in the wall thickness of the pipe as

effective corrosion mitigation measures will be provided in the system

344 Pipes of higher wall thickness are envisaged to be laid across major rivers water

courses etc At Rail and Road crossings casing pipes will be provided for additional

safety of the carrier pipes

345 Horizontal Directional Drilling (HDD) will be carried out at all major river

crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction

411 This chapter broadly deals with various features of the project viz pipeline sizing

pipeline route system configuration facilities required cathodic protection

telecommunication amp telesupervisory system implementation methodology

construction schedule operation philosophy etc

42 Pipeline Sizing

421 The pipeline system has been designed for optimal transportation of petroleum

products Pipeline size selection has been carried out based on findings of detailed

route survey as well as short term and long-term throughput projections Accordingly

18rdquo OD x 025rdquo WT API 5L-X70 Grade pipe has been considered for design

43 Hydraulics and System Configuration

431 Based on the pipeline throughput requirements the pipeline system has been designed

for implementation in 2 stages Hydraulic have been worked out for both the stages

Details are as under

Stage Design Capacity (MMTPA)

Flow Rate (klhr)

Originating Station

IPS Delivery Station

Terminal Station



Line Size MAOP







Hydraulics

Stage-I

S No Station Chainage (km)

Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50

km Kilometre m Metre mcl Metre Column of Liquid (HSD) SDH Station Discharge Head RH Residual Head IPS Intermediate Pump Station MLPUs Main Line Pumping Units

Note - In Stage-I Bolpur will be designed considering a scrapper station and the same will be converted to pump station in Stage-II

Hydraulic gradient is placed at Annexure-I

44 System Requirements

441 The new pump station will be constructed at newly acquired land (20 acre) near

existing HBCPL Haldia station and new pipeline will originate from this pump

station The booster pump station will remain at the existing pumping station (located

inside Haldia refinery) However the existing booster pumps will be replaced with

higher capacity booster pumps

Stage-I configuration of the pipeline system broadly comprises the following

Laying of 535 km 18rdquoOD x 025rdquo WT API-5L-X70 Grade pipe from proposed

new mainline pump station at PHBPL Haldia to the existing terminal station at

HBPL Barauni




Replacement of 2 booster pumps (1+1) at existing booster station at HBPL

Haldia

Installation of 3 motor-driven MLPUs (2 operating + 1 standby) at new pump

station at HBCPL Haldia

Laying of about 10 km 18rdquoOD x 0281rdquo WT pipe from existing pump station

at HBPL Haldia to proposed new mainline pump station at HBCPL Haldia

Scrapper station at Bolpur

Hookup with existing marketing terminal at Jasidih

Total No of Mainline SVs (including River MOVs) envisaged is 41

Station facilities modifications at Barauni to accommodate increased

throughput requirement

Conversion of 1 LBT Tank of 3500 kl capacity at Barauni from HSD to MS

service

442 The facilitiesMLPUs designedprocured for Stage-I will be adequate to meet the

configuration of both Stage-I amp Stage-II

443 In Stage-II configuration the scrapper station at Bolpur will be converted into

pumping station by installing 3 motor-driven MLPUs

444 After commissioning of this pipeline the existing intermediate pump station at

Asansol would become redundant and would be de-commissioned Mainline pumping

units at Asansol would be suitably utilized at some other pipeline location as per

requirement

Schematic flow diagram of the pipeline system is shown in Annexure-II

45 Additional Refinery amp Marketing Facilities at Haldia

451 Additional facilities at Haldia refinery will involve engineering and execution of a

new common 18 inch discharge header for hooking up with the existing booster pump

discharges from refinery tanks and laying of this pipeline up to HBPL boosters

452 Additional marketing facilities at Haldia Jasidih will involve modification to existing

pipes valves amp flanges etc to accommodate higher flow rate




452 Engineering and execution of the above facilities will be carried out by respective

Divisions Estimated cost towards these additional facilities has been incorporated in

the capital cost

46 Pipeline Route

461 Pipeline will originate from PHBPL pump station at Haldia The new pipeline would

be laid in common RoW of PHBPL up to Bolpur station (ch 206 km) from Haldia

Thereafter it will travel in new RoW via Jasidih from ch 206 km to ch 465 km

Subsequently from ch 465 km to ch 535 km the pipeline will follow the existing

RoW of PHBPL Existing HBPLHMRBPL pump station is in the Haldia refinery

premises which is about 10 km away from PHBPL Haldia pump station The existing

common RoW from HBPL booster station to PHBPL will be used for the proposed 10

km pipeline and additionally approx 2 km of pipeline would be required in new RoW

for hooking up with new station at PHBPL Haldia Route map is attached as

Annexure-III

462 The proposed Haldia-Barauni product pipeline traverses through 5 districts of West

Bengal covering a length of 267 km and 2 district in Jharkhand covering a length

120 km and also traverses through 5 districts of Bihar covering length of 148 km The

proposed pipeline alignment generally runs in North West direction

463 The terrain along the pipeline route is mostly flat and rolling The agricultural crop

grows in the region are mostly Paddy

464 The proposed Haldia-Barauni pipeline will not pass through any ReservedProtected

forest all along the route Although reserve forest has been avoided in fixing the

pipeline alignment village forests and forest in Government land along the proposed

pipeline alignment may be encountered This aspect will be known only after carrying

out detailed engineering survey of the proposed alignment

47 Civil

471 Provision of land acquisitionpurchase has been kept only for new RCPSV stations

along the mainline route Land acquisitionpurchase has been envisaged for Scrapper




station Intermediate Station at Bolpur The size of proposed plan has been considered

as 250m x 130m

472 Civil structures are envisaged at all locations to house men and machinery Pump

sheds and booster sheds required to accommodate the pumping units with associated

facilities have been planned to be of steel structure RCC structures are required to

house control panels MCC panels HTLT panels batteries etc All the safety factors

like wind load seismic load soil bearing capacity etc would be taken into account

while designing the civil (Steel amp RCC) structures

473 The following facilities have been considered for Jasidih

SRB - Foundation SLB - Foundation pipe and valve supports LT Room CP Room

Battery Room Telecom Room Roads Drains Pathways etc

Existing infrastructure of Control Building MCCPCC Building StoresWorkshop

will be used for operation

48 Cathodic Protection System

481 Temporary Cathodic Protection (CP) system with the requisite design life is envisaged

during the construction works using the Mg anodes in line with OISD guidelines

482 Cathodic Protection system will consist of 11 nos of CP units for the protection of

535 km mainline and 3 nos of CP units for the protection of station piping at Haldia

Bolpur amp Barauni stations

483 Out of 11 Mainline CP units 5 nos of CP units (with battery back-up) will be

positioned in mainline at isolated locations (RCPSV) where power supply

arrangement is being considered from SEBs and remaining 6 nos CP units for

protection of mainline will be positioned inside stations

49 Details of Facilities in Stage-I

491 Mechanical

4911 Two motor-driven booster pumps (1 operating + 1 stand by) at existing HBPL Haldia

station and 3 MLPUs (2 operating + 1 stand by) having variable frequency drive

(VFD) have been considered at the originating pump station at proposed new




pumping station near HBCPL Haldia In addition one 20 kl sump tank a skid

mounted OWS of 10klhr capacity Separator filters and 12rdquo fire water hydrant

network considered for new facility The proposed hydrant network will be connected

with existing fire water network of COT at Haldia

4912 Installation of scrapper receiving and launching barrels of 18x22 of 600 has been

considered at Haldia Bolpur amp Barauni

4913 Installation of scrapper receiving and launching barrels of 18x22 of 600 along with

hook-up of Mainline with existing station facilities has been considered at Jasidih

492 At Barauni 2 transmix tanks of 1000 kl each (for MS amp HSD service) one 20 kl

sump tank a skid mounted OWS of 10 klhr capacity Separator filters and 12rdquo fire

water hydrant network has been considered for new facility The facilities for

injecting the interface from transmix tanks to product delivery lines (HSD and MS)

transferring unabsorbed interface from transmix tanks to crude oil pipeline of HBCPL

have been considered at Barauni The proposed hydrant network will be hooked up

with existing fire water network of Barauni pumping station

493 Pipes pipe fittings flanges etc will conform to International Standards such as API

5L ANSI B-165 ANSI B-1625 WPB-234 MSS-SP-44 MSS-SP-75 etc and will

be suitable for ANSI-150 and 600 pressure classes Gate valves ball valves swing

check valves will conform to API 6D standards Electric motor actuators of suitable

power ratings will be installed for the operation of gate and ball valves

494 The mainline pumps would be conforming to API 610 standard They would be fitted

with mechanical seals conforming to API 682 std and coupled with Horizontal

Flame proof weather proof Electrical Motors These Motors would be provided with

VFD

495 The DFR considers utilization of existing facilities available within refineries and

Marketing terminal through appropriate hook-up with the existing network

Accordingly no separate fire water storage tanks pumping units etc have been

considered at Haldia Jasidih and Barauni




410 Electrical

4101 Haldia Booster Station

41011 Power supply of 66 kV shall be made available from Haldia Ref HMR New HT

Panel has been envisaged for new Booster motors with Soft Starter Panels Presently

power supply is coming from State Electricity Board at HMR Haldia Accordingly

provision of HT DG set has been envisaged at Haldia Booster Station

41012 LT Power supply for new facilities shall be arranged from HMR Haldia and new LT

Panel has been envisaged

41013 Facilities like MOVrsquos HTLT MCC Panel High Mast have been considered

41014 Electrical power of approx 800 KVA for BPMOVLightingMainline CP etc shall

be provided by existing incoming Power supply 66kV0415kV through existing

HMR Haldia Haldia Refinery

4102 Haldia Mainline Pumping Station

41021 66 kV Power supply shall be made available from PHBPL Haldia switchyard under

PHDPL Project with addition of 1 additional 125MVA Bay

41022 LT Power supply for new facilities shall be arranged from new 660415kV

500KVA Transformer at Haldia and new LT Panel has been envisaged

41023 Facilities like MOVrsquos HTLT MCC Panel High Mast etc have been considered

41024 Electrical power of approx 2400 KVA for MLPUMOVLightingMainline CP etc

shall be provided by existing incoming Power supply 33kV from WBSEDCL

through 3366kV 125MVA Switchyard at Haldia by means of an additional bay at

Haldia New Transformer of 660415kV 500KVA has been considered for catering

to LT Loads HT LT DG sets have been envisaged

4103 Bolpur Station

41031 Existing Contract demand is 400KVA at 11kV Supply Voltage additional load

requirement of 100 kVA shall be made from existing supply




41032 LT Power supply for new facilities shall be arranged from SEB and new LT Panel has

been envisaged LT DG set 415V 500KVA has been envisaged


4104 Jasidih Delivery Station

41041 Mains power supply of 40KVA at 415V voltage level shall be arranged from existing

Marketing TerminalPL Terminal at Jasidih

41042 LT Power supply for new facilities shall be arranged from Jasidih and new LT Panel

has been envisaged LT DG set has been envisaged

41043 Facilities like MOVrsquos LT MCC Panel High Mast etc are required and have been

considered

41044 Electrical power of approx 40 KVA for MOVLightingMainline CP etc shall be

provided by existing incoming Power supply 415V from Pipeline facilities through

Marketing terminal at Jasidih

4105 Barauni Terminal Station

41051 Mains power supply of 80 kVA at 415V voltage level shall be arranged from existing

Marketing TerminalPL Terminal at Barauni

41052 LT Power supply for new facilities shall be arranged from Barauni and new LT Panel

has been envisaged LT DG set 415V 100KVA has been envisaged

41053 Facilities like MOVrsquos LT MCC Panel High Mast etc have been considered


required which shall be provided by existing incoming Power supply 415V from

Marketing terminal at Barauni

411 Details of Facilities in Stage-II

4111 At Bolpur three motor-driven mainline pumping units (2 operating + 1 stand by)

having variable frequency drive (VFD) along with 12rdquo delivery manifold a skid




mounted OWS of 10klhr capacity and 12rdquo fire water hydrant network has been

considered for new facility The proposed hydrant network will be hooked up with

existing fire water network of Bolpur station

4112 3366kV 10MVA Switchyard is required for catering to power supply from SEB

HT DG set of 66 kV 2 MVA has been envisaged

412 Instrumentation and Station Control Centre

4121 Instrumentation will be provided to cater for operation and control to optimise the use

of equipment and manpower and to protect the equipment All stations will be

provided with hot standby PLC based station control system (except block valve

locations where non-redundant RTUs shall be provided) to perform local control

functioning and to monitor and report local conditions

4122 The field instrumentation at station comprises of pressure transmitter pressure

switches pressure gauges mass flow meters Ultrasonic flow meters flow switches

level switches level transmitters density meters temperature transmitter scrapper

detector emergency shutdown switches etc

4123 Mass Flow Meters have been considered at originating and delivery stations and

ultrasonic flow meters have been considered at Intermediate pump stations

4124 Station Control Centre (SCC) shall have Workstations system as operator interface to

the station instrumentation and control system The computers shall be connected to

dual local area networking (LAN) in client server mode They shall work in hot

standby configuration and shall be connected to the PLC control system over LAN

They shall be interfaced with the PLC system on continuous basis for monitoring of

station parameters and control The SCC computers shall have several graphic screens

depicting the station pipeline network and several equipments in the station

Operators shall monitor operate and control the station equipments and parameters

through graphic screens in the computers All alarms events status of equipment etc

shall be logged in the computer system and periodic on demand print out as hard

copy shall be possible through printers connected on LAN




4125 Jasidih is an existing delivery station where scrapper facilities and hook up with

existing delivery facilities are proposed under the project The existing control system

of Jasidih will continue to be in use and will be hooked up with the new pipeline

SCADA system through a new RTU which is considered at Jasidih

4126 The system power supply shall be through UPS system with battery backup for round

the clock uninterrupted operation

4127 The Station Control Centrersquos shall be connected to the Master Control Stations

through LAN and WAN for SCADA operation

413 Telecommunication System

4131 A dedicated state of the art OFC based STM-16 25 Gbps SDH (Synchronous Digital

Hierarchy) communication system with 999 availability is envisaged SDH is a

standard technology for synchronous data transmission on optical media (Optical

Fibre Cable) SDH uses the various Synchronous Transport Modules (STM) and data

transmission rates such as STM-1 (155 Mbps) STM-4 (622 Mbps) amp STM-16 (25

Gbps)

Out of total 535 km of mainline new OFC shall be laid for approx 472 km and for

balance ie in Khana-Bolpur amp Dumri-Barauni sections the OFC being laid under

the PHBPL- Aug project will be utilised for the communications

4132 For the entire communication network of the pipeline the following type of stations

have been considered -

Attended Stations 4 Nos (Haldia Bolpur Jasidih amp Barauni)

RCP Stations 3 Nos

SV locations 37 Nos

4133 RTU data amp CCTV requirements of SV locations considered all along the pipeline

shall be catered by the network connectivity using fibre of the OFC network

4134 The NMS (Network Management System) for the SDH network is planned at




Haldia to monitor amp configure the telecom network hardware from centralised

location

4135 It is proposed to install IP amp E1 based new EPABX Systems at all manned locations

to provide dedicated voice communications for operations

4136 The power requirement of equipment shall be met with the power systems (Battery

charger + battery bank) at all manned locations At RCP locations amp SV locations

dedicated battery chargers with battery bank + Solar System have been considered

4137 CCTV based Surveillance system has been considered for all manned stations as

well as RCPSV locations

4138 Control Centre for CCTV System has been envisaged at Haldia for monitoring amp

recording of CCTV cameras for whole pipeline section This feed shall be available

over LAN at all stations on Ethernet

4139 VHF System (Base Station + 8 nos hand held sets for originating pumping stations

and 6 nos hand held sets for delivery stations) have been considered for all manned

locations

41310 No Telecom equipment (except network switches telephone instruments VHF sets)

has been considered at Booster station inside Haldia Refinery Only OFC laying

(approx 7 km) has been considered for SCADA connectivity which shall be

achieved on OFC through network switches However CCTV system has been

considered for Haldia booster station

414 Telesupervisory (SCADA) System

4141 The Tele-supervisory system for the proposed pipeline is envisaged to have dual hot

stand-by computer system in client-server mode sitting on dual local area network

(LAN) for round the clock monitoring and control of pipeline from a centralised

location called Master Control Station (MCS) In the event of failure of the duty

machine the hot stand-by machine will take over the role of the duty machine

instantaneously without affecting the operational continuity and loss of data

thereby ensuring high reliability of the system The tele-supervisory system will




work in Master-Slave configuration having its slave stations at attended stations

and at block valve locations installed along the entire pipeline network The master

station shall be interfaced with slave stations over OFC telecom system over Wide

Area Network (WAN) for data acquisition and control

4142 RTU has been considered for all RCP amp Block valve locations to control amp monitor

the local facilities from remote centralized master location

4143 It is envisaged to have Master Control Station at Haldia Station The Master Control

Station shall be equipped with Supervisory Control and Data Acquisition (SCADA)

software running under multi-programming multi-tasking real time operating

system environment The SCADA software shall incorporate control amp monitoring

of all locations including Block valves Backup Master Control Station has not been

considered in the project as total length of pipeline is only 535 kms

4144 Leak Detection system has been envisaged for complete section of the Pipeline

Leak Detection Software shall run in a separate machine at Master Control Station

This package will enable the operator to take optimal control actions and thus

ensure the safety and security of the pipeline network

415 Fire amp Gas Detection Facilities

4151 Safety PLC based fire amp gas detection system along with hydrocarbon detectors amp

UVIR Flame detectors have been envisaged at all attended stations (including

booster station inside Haldia premises)

4152 Fire Alarm Panel along with multi-sensor amp heat detectors have been considered at

attended stations At Block Valve locations hydro carbon detectors multi-sensor

detectors etc have been considered as per requirement

4153 FM200 based Fire extinguishing systems have been considered for Control rooms of

all attended stations

4154 CO2 based (which will be reviewed during detailed engineering stage) Fire

extinguishing systems have been considered for HT VFD buildings and Equipment

rooms of all attended stations




416 Operation philosophy

4161 Delivery of products to depots can be through heart-cut or blocked out mode as per

the requirement but considering that 85 of total pipeline throughput to be delivered

at Barauni the facilities have been designed for blocked out delivery to Barauni The

typical pumping sequence in the pipeline would be as under




4171 Minimum batch length for MS and HSD has been worked out considering

simultaneous delivery at Jasidih and Barauni Considering absorption of 1 SKO in

MS and 1 SKO in HSD minimum batch length required is 30000 kl and 33000 kl

for MS and HSD respectively Considering the small delivery volume at Jasidih

interface absorption of entire batch will be done at Barauni Batch length of SKO

would depend on its requirement However a minimum PCKSKO plug of 1000 kL

would be required for absorption of interface

4172 In case of non-availability of MSHSD batch as above or due to unplanned shutdown

of the pipeline interface might increase in the pipeline and some unabsorbed

interface may be there which would be delivered in the transmix tanks at Barauni

MS-PCKSKO interface would be received in MS Transmix tank and HSD-

PCKSKO interface would be received in HSD transmix tank A part of the interface

received in transmix tanks may be blended online in the products being delivered in

tanks at Barauni Remaining part of the unabsorbed interface if any from transmix

tank would be pumped to crude oil delivery header of PHBPL Barauni for blending

in crude oil and further processing by Barauni Refinery Facilities for the same have

been considered at Barauni

4173 Tankages

41731 LBT-04 of gross capacity of 3500 kl which is a FR tank at Barauni being used in

HSD service will be changed to MS for pipeline operation






419 Condemnation

4191 The existing 1275OD pipeline would continue to remain in use till completion of

proposed scheme

4192 Upon successful commissioning of new pipeline action would be initiated for

condemnation of existing pipeline

4193 The existing intermediate pumping station at Asansol would be redundant and would

be decommissioned Mainline pumping units at Haldia amp Asansol would be suitably

utilized at some other pipeline location as per requirement


4201 Suitable action will be taken for obtaining MoEampF clearance and other statutory

clearances for the proposed pipeline from concerned authorities as applicable


4211 The proposed scheme is expected to be completed in a period of about 36 months

after receipt of statutory clearances Construction schedule is enclosed in

Annexure-IV


4221 The manpower requirement would be about 67 during construction phase excluding

Line Patrolmen (LPM) The requirement of manpower is expected to be met through

internal deployment as well as by induction of competent personnel The

requirement of LPM for new RoW is envisaged to be outsourced

4222 The existing manpower at Haldia Jasidih and Barauni would be adequate to handle

the operating phase and manpower presently stationed at Asansol would be suitably

re-deployed

SAFETY HEALTH amp ENVIRONMENT




CHAPTER -V

50 Safety Health amp Environment

51 Pipelines Division of Indian Oil Corporation Limited owns and operates over 11000

km of pipeline network as of now Safety aspects have always been given prime

importance in all spheres of pipeline construction works operation amp maintenance

including pipeline system design

52 IOC has always accorded high priority to Health Safety and Environment (H S

ampE) Safety Management is an integral part of overall management system of the

company right from the inception IOC is committed to safety and demonstrated

leadership in the field of Health Safety and Environment The H S ampE policy of

IOC demonstrates this commitment To achieve the overall objective and to provide

safety care for health and clean environment IOC has departments at corporate

office Refinery units Pipelines amp Marketing installations and at Regional State

levels as well as in RampD Centre

53 Safety amp Fire Protection Measures

531 IOC has a well-defined H S ampE Policy approved by the Board which gives

direction for various safety occupational health and environment protection related

activities Adequate resources are allocated for effective implementation of H S ampE

policy to achieve high standards of safety Safety Committees play vital role in this

regard Representatives of the workmen and officers work together in the Safety

Committees

532 It is the endeavour of the management to involve all the employees and others

related personnel in the safety matters Safety is a key element reviewed in the Local

Management Committee Meetings chaired by Unit HeadInstallation Head

Management Safety Committee Meeting is held every quarter under the convenor

ship of Unit HeadInstallation Head to review all aspects of safety Respective

Divisional Director reviews safety performance in their monthly Performance

Review Meetings of the Divisions




533 Board of Directors are appraised on safety performance with respect to

implementation of recommendations made by External Safety Audit (ESA) teams on

regular basis Major incidents and corrective actions taken are also appraised to the

Board Executive Committee of the Board is apprised on safety issues of the

corporation on quarterly basis

534 Process hazards are reviewed at all phases of project life Multidisciplinary team

carries out these reviews For identification assessment and control of process

hazard Hazard and Operability (HAZOP) study and Risk Analysis are carried out

Quantitative Risk Analysis (QRA) is carried out for any new unit or facilities

Actions are taken on the basis of QRA to mitigate or minimize the hazards

535 Standard Operating Procedures ensure correct operations and are updated

periodically Only trained manpower can ensure safe operation IOC train all

concerned including employees contractor labourers truck drivers and security

personnel etc Considering the socio-economic conditions and high turnover of

contractor personnel major thrust is given for training of contractor personnel

536 For new projects pre-commissioning checks and audits are carried out by multi-

disciplinary teams and deviations if any are corrected before start up Also pre-

commissioning audit is carried for new plants and pipelines by the Oil Industry

Safety Directorate (OISD) a technical directorate under Ministry of Petroleum amp

Natural Gas Government of India

537 Mechanical Integrity of equipment system is ensured through condition monitoring

periodic inspection and preventivepredictive maintenance for reliable and safe

operation All incidents are investigated with the objective of learning and to avoid

repetitive mistakes Recommendations are implemented in time bound manner

538 All jobs in the plants are carried out through a systematic Work Permit System to

ensure that safety precautions are taken in line with the norms guidelines of OISD

Use of proper Personal Protective Equipment (PPE) is enforced Strict supervision is

maintained by Fire amp Safety Personnelsite supervisors regarding compliance of

permit conditions and use of PPE




539 The company has elaborate fixed as well as mobile firefighting equipment and

system backed by dedicated Fire Fighting crew to take care of

emergencieseventualities Also a well-structured Emergency Management Plan at

each location has been devised to meet these requirements System effectiveness is

ensured through regular mock drills Health of the facilities are ensured through

periodic inspection maintenance and testing Agreements are in place with

neighbouring industries and District Authorities for Mutual Aid On-site and Off-site

Disaster drills are conducted as per calendar

5310 To ensure effectiveness of all the component of our safety system and activities the

following audit systems are in place

Internal Safety Audit by multi disciplinary teams

External Safety Audit by OISD

Surprise Safety Check by OISD

5311 H S ampE performance of contractors and business associates has direct bearing on

their ethics safety orientation and policy towards Health Safety amp Environment and

good contract management To ensure contactor and contract workmen safety the H

S ampE performance of the contractor is assessed while doing pre-bid evaluation

5312 Inclusion of guidelines on safety in the tendering stage itself like General Conditions

of Contract (GCC) Special Conditions of Contract (SCC) ensures safety standard

during execution of the contract

5313 It is ensured that the contractor provides adequate means and establishes a suitable

programme on safety amp health for workers consistent with NationalState laws and

regulations

5314 OISD guideline OISD-GDN-192 on ldquosafety practices during constructionrdquo forms a

part of the tender document The objective of this guideline is to provide guidance

on technical and educational framework for safety amp health in construction

5315 Along with Strong Safety Management System adequate fire protection and fire

fighting facilities have been provided Major system facilities are outlined below




bull Dedicated Fire fighting protection facilities are designed as per OISD norms

which are based on reputed international codes like American Petroleum

Institute (API) USA National Fire Protection Association (NFPA) USA

Institute of Petroleum (IP) UK etc as well the industry experience

bull Fire fighting facilities including water storage and the pumping capacities are

designed to take care of two fires simultaneously anywhere in the unit for

major installation having storage more than 30000 KL and at Refineries

Petrochemicals

bull Pressurized hydrant system is provided throughout the premises

bull Sufficient number of mobile firefighting equipment like foam fire tenders

foam nursers Dry Chemical Powder tenders mobile monitors etc have been

provided at UnitInstallations as per requirements

bull Centralized control rooms are equipped with modern communication

facilities like walkie-talkie pagers etc for prompt action in case of any

emergency Emergency call point systems have been provided at strategic

places around the plant area and siren for sounding emergencies

bull Plant and security personnel are trained to supplement fire fighting rescue

operation during emergencies

bull Water spray system sprinklers are provided in vulnerable areas like storage

tanks columns and hot pumps Semi-fixed foam system has also been

provided in storage tanks storing crudepetroleum products

bull At LPG plants automatic water spray system and Remote Operated Valves

at LPG Horton spheres for quick isolation in times of emergency have been

provided

bull Gas Hydrocarbon Detectors are provided in LPG area and other vulnerable

areas for early leak detection




bull All Fire Fighting and Safety equipment are inspected and maintained

regularly to keep them always in operational readiness

bull Mock fire drills are conducted every month for creating safety awareness

bull Off-site mock drills are conducted in pipeline RoW

5316 The objective of adhering above mentioned lsquosafety aspectrsquo is to provide practical

guidance on technical and educational framework for safety in different areas of

pipeline activities with a view to prevent accidents and to provide safety practice

guidelines for appropriate measures of planning control and enforcement

54 Environment Management

541 Environment Management is a priority area for IOC by continuously striving to

minimize adverse environmental impacts from company activities products and

services by using processes practices materials and products that avoid reduce or

control pollution Following measures are taken for control and abatement of

pollution

542 Waste Water Management Our refineries and large crude oil storage terminals are

equipped with well-designed Effluent Treatment Plants (ETP) In Marketing and

Pipeline locations effluent water is routed through oil water separator

543 Water Conservation The treated effluents are reused recycled for various

purposes like fire water amp cooling tower make up captive irrigation in our green

belts amp Eco parks and make up to Eco- ponds This has helped in reducing discharge

of treated effluent outside and to that extent fresh water consumption for operations

Rainwater harvesting is done in all installations

544 Prevention of Air Pollution Refineries are monitoring ambient air quality at fixed

monitoring stations Mobile van equipped with sophisticated monitoring equipment

is also in use In Marketing installations all vehicles under contract are required to

have PUC certificates and these are checked routinely and during inspections




545 Tree plantation Eco-park Tree plantation in and around installation and

development of green belts ecological parks has been a significant feature of

IndianOilrsquos operations All refineries have developed green cover around their

operations Extensive tree plantation is carried out in Marketing amp Pipelines

installations and RampD Centre

546 Clean Development Mechanism (CDM) Monitoring and control of emission of

Green House Gases Mainly Carbon Dioxide is being done Clean Development

Mechanism (CDM) projects are also under implementation in Refinery Units

55 Oil Spill Response (OSR) Facilities

551 Prevention of oil spills whether on land or water (including both sea and fresh

water) has always been on top of IOCrsquos business endeavors This concern does

include all possible sources of oil leak including oil tanker spills non-tanker ship

spills pipelines from SBM to onshore tanks and tank farms or may be cross country

crude oil as well as product pipelines

552 IOCL largely depends on crude imports through VLCC and other tankers which are

unloaded through SBM IOCL believe that any major oil spill at these locations does

have the potential to cause serious problems for coastal and marine wildlife

especially corals fishes birds mammals and reptiles

553 Tiered preparedness and response gives a structured approach to both establishing

oil spill preparedness and undertaking a response It allows potential oil spill

incidents to be categorized in terms of their potential severity and the capabilities

that need to be in place to respond Conventionally the concept has been considered

as a function of size and location of a potential oil spill with three tiers typically

defined

554 As a responsible Corporate citizen IOC is fully aware of its responsibility towards

not only mitigating environmental pollution due to its operations but also the role it

can play in improving the environment by making products which cause least

pollution and towards this end has made massive investments in setting up necessary

infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST

61 The pipeline system from Haldia to Barauni is estimated to cost Rs1038 crore

including a foreign exchange component of Rs8 crore at November 2015 price

level This comprises Rs1021 crore towards cost of the pipeline system Rs11 crore

towards modification to existing piping valves etc at the existing Haldia and Jasidih

Marketing Terminal and Rs6 crore towards modification to existing pipes valves amp

fittings etc at Haldia refinery

62 The cost estimates has been prepared after preparing process flow diagram PampIDs

and tentative layouts based reconnaissance survey thereby establishing reasonable

requirements of facilities in line with the overall project scheme and experience of

setting up identical similar projects

63 Estimation of quantities and costs of all items related to pipeline survey materials and

construction electrical and mechanical items have been worked out based on

approved standard Schedule of Rates (SOR) with appropriate escalation as per

CPIWPI index whichever is applicable

64 Materials amp Work items for which standard SOR rates are not available have been

estimated by appropriate pro-rating with items that are available in standard SOR or

with unit costs of similar previously awarded purchase orders

65 The project cost for additional facilities at Haldia refinery has been furnished by

Refineries Division

66 Survey and Field Engineering

661 This cost includes the cost of surveys sub-soil investigation amp field engineering

67 Land Acquisition RoW and Crop Compensation

671 RoW compensation has been considered for a new 18m wide strip along the pipeline

while crop and forest compensation have been suitably considered Costs related to




land requirement process has been considered for scraper station at Bolpur mainline

SVs and RCPs only

68 Project Management amp Engineering


after receipt of statutory clearances The cost of project management amp engineering is

estimated on the basis of envisaged time schedule

69 Mainline Pipes amp Materials

691 The cost of pipe and coating has been considered as per the latest available data The

cost of mainline materials required such as casing pipe coating and wrapping

materials valves etc has been estimated on the basis of SOR

610 Mainline Construction

6101 The cost of mainline construction has been estimated on the basis of the standard

SOR in recent past for similar items

611 Pump Station and Terminal

6111 Cost under this head includes the cost of mechanical civil electrical and

instrumentation amp control facilities which mainly comprise the mainline pumping

units including prime movers valves sump pump amp motor scraper barrels fire alarm

amp detection system fire hydrant network amp related facilities Power-cum-Motor

Control Center PLC based control system control buildings etc including the

erection and installation of requisite facilities

612 Cathodic Protection

6121 This includes the cost of materials required for temporary and permanent cathodic

protection installation amp commissioning of equipmentmaterials CP rectifier units

ground beds cable etc Estimates are based on standard SOR and rates from similar

projects executed in the recent past wherever items are not available in SOR




613 Telecommunication and Telesupervisory System

6131 This includes costs pertaining to OFC based telecommunication systems RTUs

CCTV based monitoring systems and other telecommunication systems to be

provided at all manned and unmanned stations Cost estimates are based on standard

SOR and rates from similar projects executed in the recent past wherever items are

not available in SOR

614 Escalation

6141 No provision has been made for price escalation during the period of execution of the

project However provision for contingencies to the tune of 5 has been made in the

cost estimate which is considered to be adequate to cover unforeseen factors

615 The summary of capital cost is given in Annexure-V

OPERATING COST




CHAPTER - VII

70 OPERATING COST

71 Operating cost of the pipeline system includes the incremental cost of powerfuel for

mainline pumping units utilities consumables and full repair and maintenance for the

proposed pipeline etc

72 The incremental operating cost for the pipeline for Stage-I is estimated to be about

Rs19 crore per annum at November 2015 price level No additional manpower cost

has been considered for the proposed HBPL as the existing manpower will handle the

operating phase Details of the operating cost are given in Annexure-VI

73 FuelPower (Electricity)

731 Cost of power for prime movers of mainline pumps and station electrical

consumption has been considered Rs833 per unit

74 Utilities

741 Power is also required for operation of auxiliaries controls etc and for illumination at

stations Requirement of power is planned to be drawn from Haldia refineryJasidih

Marketing TerminalSEB

742 There is no major requirement of water for operation of the pipeline system Water

for firefighting will be drawn from the existing fire water networks of Haldia refinery

and Marketing terminals at Jasidih

75 Manpower



re-deployed




76 Repair and Maintenance

761 Repair and maintenance of mainline has been considered to be about 1 of the

investment in the mainline Similarly repair and maintenance of stations has been

considered to be about 2 of the investment on stations and telecommunication amp

telesupervisory system

FINANCIAL ANALYSIS




CHAPTER - VIII


81 Project Financing

811 Capital cost of the project is considered to be financed through internal

resourcescommercial borrowings For the purpose of financial analysis debtequity

ratio of 11 has been considered with interest 940 per annum and repayment in 8

equal instalment with one-year moratorium from the date of commissioning

Requirement of working capital will be met through internal resources

82 Financial Analysis

821 Financial analysis for the proposed pipeline system has been carried out for Stage-I

facilities taking into account the following

Incremental throughput and corporate saving

Capital cost of the pipeline and its operation for 25 years

Throughput as indicated in the optimization study for 2018-19 and 2021-22

Corporate savings assessed in the optimization study as revenue

Benefit due to lower transit loss in pipeline transportation compared to typical

losses permitted for transportation through other modes of transportation

Savings in loadingunloading charges



144 167




83 Sensitivity analysis has also been carried out the results are as under

Case IRR [ROI ()] IRR [ROE ()]

Increase in capital cost by 10 133 151 Increase in operating cost by 10 142 164 Decrease in throughput by 10 131 148 All of the above together 119 131

84 From the above it can be seen that the calculated IRR is higherequal to the current

hurdle rate of 12 (for pipeline projects) in all scenarios and the project is financially

viable The pipeline will facilitate cost-effective transportation of products from

Haldia to the major consumption centre in the state of W Bengal Jharkhand Bihar

and UP vis-agrave-vis other mode of transportation

CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX


91 The products from Haldia refinery coastally received are transported through HBPL to

the demand centers in W Bengal and Jharkhand and also Barauni for further movement

through BKPL for the ToPs in Bihar and UP

92 The existing HBPL is in operation for more than 48 years and during this period its

health condition has been deteriorated significantly The pipeline has history of

leaksfailures Presently the pipeline is being operated at derated pressure due to these

reasons

93 However even after re- routing of existing pipeline section of HBPL which is passing

through the coal belt area around Asansol there will not be any increase in throughput as

the pressure of pipeline sections upstream and downstream of this pipeline section would

be restricted to the derated pressure and to meet the demand of the consumption centers

fed through HBPL a new pipeline would also be required

94 Accordingly a new pipeline is proposed from Haldia to Barauni which will not only

ensure meeting the enhanced throughput requirement which is required in next 5 years

but would also eliminate the probability of subsidence and in-service failure of the

pipeline

95 HBPL is a critical link for supply of products from ParadipHaldia refinerycoastal inputs

at Haldia to demand centres in Bihar UP and Jharkhand Derating of the pipeline and

leaksfailures have resulted in restricted capacity of existing pipeline and the present

product positioning arrangement would not be adequate in meeting the future demand in

a reliable and cost-effective manner

96 It may be observed that even after considering maximum achievable capacity the

existing HBPL system would not be sufficient to meet the throughput requirement in




short-term (21 MMTPA) as well as long-term (40 MMTPA) scenarios which otherwise

would necessitate laying of another pipeline or else would result in un-economic supply

of products to BKPL ToPs by rail transportation



for operational safety of pipeline amp capacity restrictions in existing pipeline for meeting

the short-term as well as long-term throughput requirement it is prudent to lay new

product pipeline from Haldia to Barauni

98 This pipeline will ensure cost-effective transportation and uninterrupted supply of

petroleum products of IOC from HaldiaCoastal input in short-term and from Paradip

through proposed PSHPL in long-term to Marketing Terminals in UP Bihar and

Jharkhand thereby maintaining IOC market share capturing new market areas in UP

Bihar and West Bengal

99 In view of the inherent advantages of pipeline transportation as discussed above and the

estimated economic benefits it is recommended to lay a new Haldia-Barauni product

pipeline at an estimated cost of Rs1038 crore including a foreign exchange component

of Rs8 crore at November 2015 price level This comprises Rs1021 crore towards cost

of the pipeline system Rs11 crore towards modification to existing piping valves etc at

the existing Haldia and Jasidih Marketing Terminal and Rs6 crore towards modification

to existing pipes valves amp fittings etc at Haldia refinery

910 Results of the financial analysis indicate that the proposed pipeline is viable considering

the prevailing hurdle rate of 12 The analysis has been done considering incremental

throughput and corporate saving

911 The current approval is being sought for implementation of Stage-I of facilities Stage-I

will be implemented first and a separate proposal will be put up for Stage-II subsequent

to the successful commissioning and realization of projected throughput as envisaged in

Stage-I




912 The project is estimated to be completed in a period of about 36 months after receipt of

all statutory clearances

913 Accordingly this DFR is submitted for approval of the Board to the above

recommendations

--- ---

ANNEXURE amp APPENDICES

0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5

Barauni Annexure - I

Hydraulic Gradient Haldia-Barauni Product Pipeline

211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46

MAOP=1158 mcl (98 kgcm2)

200

385

Jasidih

176 mcl

From Haldia Refinery

Haldia PS (Ch 0 km)

Bolpur Scraper Station (Ch 206 km)

Jasidih DS (Ch 385 km)

LEGEND PUMPING UNIT (OPERATING)

PUMPING UNIT (STANDBY)

MARKETINGrsquos STORAGE TANKS

SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD

Barauni DS (Ch 535km)

Schematic Flow Diagram Haldia-Barauni Product Pipeline

18rdquo OD

18rdquo OD

18rdquo OD

535 km 18rdquo OD X 025rdquo WT API 5L X70

Asansol

Haldia

Barauni

Jasidih

Indicative Route Map

Haldia-Barauni Product Pipeline Annexure - III

SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY

1 Design and Detailed Engineering

2 Survey Land RoW Acquistion amp CropCompensation

3

4 Indenting amp Procurement of StationMaterials

5 Tendering Work Order and MainilineConstruction

6 Tendering Work Order and StationConstruction

7 Tendering Work Order and CP SystemConstruction

8 Tendering Work Order amp Execution ofTelecom Telesupervisory amp SCADAworks

9 Commissioning

LEGEND

COMMISSIONING LAND ROW amp CROP COMPENSATION ML MATERIALS amp COATED PIPES STATION CONSTRUCTION PCP WORKS

DETAILED ENGINEERING MAINLINE CONSTRUCTION STATION MATERIALS

An

ne

xu

re-IV

Haldia-Barauni Product PipelinePROJECT IMPLEMENTATION SCHEDULE

SCADA WORKS

Indenting amp Procurement of MainlineMaterials amp Coated Pipes

Page 1 of 12

Annexure-V

Haldia-Barauni Product Pipeline

Capital Cost

(November 2015 price level)

(Rs in Lakh)

No Description of Item FE Rupees Total

A Pipeline Facilities

1 Survey amp Field Engineering 0 772 772

2 Land Acquisition RoW amp Crop Compensation

0 1954 1954

3 Mainline Pipes 0 30553 30553

4 Mainline Materials 624 496 1120

5 Mainline Construction 0 23545 23545

6 Pump Station and Terminal 0 25956 25956

7 Cathodic Protection 68 1076 1144

8 Telecommunication amp Telesupervisory 0 3528 3528

Sub-total 692 87880 88572

Contingencies 35 4394 4429

Project Management and

Engineering Insurance 0 4650 4650

Total (Pipelines Facilities) 727 96924 97651

B Interest During Construction 0 4516 4516

Total (Pipelines Facilities) with IDC 727 101440 102167

C Additional Refinery Facilities at Haldia 0 545 545

D Additional Marketing Facilities at Haldia 0 1045 1045

Total 727 103030 103757

Say Rs crore 8 1030 1038

Including cost of land ie Rs682 Lakh

Annexure-VI


Incremental Operating Cost (Stage-I)


(Rs in Lakh)

S No Description of Item Cost per Annum

1 Power (for prime movers) 659

2 Utilities Power amp Water 0

3 Manpower 0

4 Repair amp Maintenance

a) Mainline 564

b) Pump Station and others 620

5

6

General Administration Expenses

Chemicals

0

40

Total 1883

(Say Rs 19 crore)

No manpower cost has been considered for the proposed pipeline

From Ganguly Subrato ( )To Mohanty Debabrata ( )Subject FW New Haldia-Barauni Product PipelineDate 10 December 2015 103541Attachments Scheme for new Barauni-Kanpur product pipelinepdf

IOM_Cost Estimate_DFR_ Barauni_kanpur_new_pipelinepdfHOLDIA -PampID-LAYOUTPDF

Regards

From Yadav Pradipkrishan ( Sent 10 December 2015 1032To Ganguly Subrato (

Cc Gupta Atul ( Sehgal Rakesh ( Durai Anna M ( Majumdar Amitava Pyne Partha (Subject New Haldia-Barauni Product Pipeline Sir Receipt at high flow rate will necessitate modification to existing pipelines valves etc atRajbandh as well as Jasidih Provision of around Rs10 Cr may kindly be made foraugmentation of Marketing facilities for facilities to be commensurate with pipelinerequirements Additional infrastructure requirements like additional storage TT loadingcapacity TW loading capacity will be undertaken by Marketing independently

( P K Yadav )General Manager (Ops) HO Mumbai--------------------------------------Off 022-26447476 Mob 8879667318

From Ganguly Subrato ( ) Sent Tuesday December 08 2015 509 PMTo Yadav Pradipkrishan ( )Subject New Haldia-Barauni Product Pipeline Dear Shri Yadav As discussed may please confirm

1 Details of existing booster pumps and pipeline size for pumping products fromMarketing installation at Haldia to HBPL

2 Whether these booster pumps and the existing lines will be able to pump 500 klshrupto the booster pumps of Pipeline installation inside Haldia refinery

In case some augmentation is required in Marketing facilities to meet the above requirementthe facilities required and cost thereof may please be sent Details received from our Haldiaoffice is also enclosed for ready reference

13

13

13

13

$

$amp

$ampampamp13

$ampamp

$amp

()+-(0

1amp

$2$

1

1()+

01amp

34(54545(5-(

13

1313 $ $amp

($ ) +

-+-

-

++-+

+00

($ )1

+132($ 0 34

5556575

-

03545(5-(67()8

-(49+54)13$

10

0

13

$

amp13 amp

( )+ -

131313

0+

0amplt

$

WATER D

RAW

LIN

E

6000 WID

E ROAD

8000 WIDE ROAD

9000 X

9000

CAP- 9

651 K

L

6000 W

IDE R

OAD

6000 W

IDE R

OAD

TANK N

O- M

13

MS

8000 WIDE ROAD

4000 W

IDE R

OAD

IN

38M D

IAX 9

6M H

T

SKO

TANK N

O- M

3

CAP- 1

0207 K

L

CR T

ANK

CLASS-B

CR T

ANK

CLASS-B

CAP- 1

0207 K

L

TANK N

O- M

2

SKO(L

S)

38M D

IA X

96

MHT

INOUT

CLASS-A

FR T

ANK

32M D

IA X

13M H

T

IN

MRN

FR T

ANK

CLASS-A

CAP- 9

651 K

L

TANK N

O- M

12

32M D

IA X

13 M

HT

FR T

ANK

TANK N

O- M

14

CAP- 1

4143 K

L

38M D

IA X

13M H

T

MS

CLASS-A

CAP- 5

430 K

L

MS

TANK N

O- M

15

CLASS-A

FR T

ANK

LT

24M D

IA X

13M H

T

DEEP T

UBE

WELL

CAP- 1

4143 K

L

TANK N

O- M

11

38M D

IA X

13 M

HT

CLASS-B

BS-II

HSD

CR T

ANK

HNG

SLOP

IN

HSD

6000 WIDE ROAD

HSD (L

SHF)

SKO

TANK N

O- M

4

CLASS-B

CR T

ANK

CAP- 1

0207 K

L

38M D

IA X

96

M H

T

LDO

TANK N

O- M

1

CLASS-C

CR T

ANK

CAP- 4

684 K

L

26M D

IA X

92

MHT

50M D

IA X

112

6M H

T

CAP- 1

8650 K

L

SEPARATOR

OIL

WATER

PUMP HOUSE

TANK N

O- M

6

SRN

FR T

ANK

CLASS-A

CR T

ANK

TANK N

O- M

5

38M D

IA X

99

M H

T

CAP- 1

0207 K

L

CLASS-C

IN

MANIF

OLD-2

DELIV

ERY

6

50M D

IA X

114

M H

T

CAP- 2

1576 K

L

TANK N

O- M

8

8000 W

IDE R

OAD

MANIF

OLD

3000 X

2000

SECURIT

Y R

OOM

HSD

BS-II

OUT

INRECEIP

T

55M D

IA X

13M H

T

TANK N

O- M

10

CAP- 2

9755 K

L

CR T

ANK

CLASS-B

8000 W

IDE ROAD

50M D

IA X

114

M H

T

CAP- 2

1576 K

L

6000 WIDE ROAD

SKO

TANK N

O- M

7

OUT

IN

ENCLOSURE W

ALL

CLASS-B

CR T

ANK

LT

SLOP R

ECOVERY

PUMP H

OUSE

3000 X

5000

6000 WIDE RO

AD

HSD

CR T

ANK

CLASS-B

OIL

WATER

SEPARATOR

6000 W

IDE ROAD

FO

FIRE BREAK WALL

IN

IN

OUT

FO

6000 WIDE RO

AD

CAP- 7

722 K

L

FO

CLASS-C

CR T

ANK

TANK N

O- M

9

30M D

IA X

114

M H

T

6000 W

IDE R

OAD

M TM2HBV2

M

TM2M

OV3TM2M

OV1

TM2G4

TM2HBV5

TM2G6

OUT

TM3G

4

TM3H

BV5

TM3G

3

TM3HBV2

TM3M

OV3TM3M

OV1

M

M

TM1G1

TM1G4

TM1G5

TM1HBV2

TM1G3

300mmDIA

80mmDIA

80mmDIA

150mmDIA

MM

TM4H

BV2

TM4M

OV3

TM4M

OV1

TM3G

6TM

3HBV

5TM

3G4

MM

TM5H

BV2

TM5M

OV3

TM5M

OV1

TM5G6

TM5HBV5

TM5G4

80mmDIA

150mmDIA

M

MTM7MOV3

TM7HBV2

RED

RED600X500500X400

TM7MOV1

TM7G

6

TM7G

4

TM7G7

TM7H

BV5

40mmDIA

M

MTM8MOV3

TM8HBV2

RED

RED

600X500

500X400

TM8MOV1

TM8G6 TM8G4

TM8HBV5

40mmDIA

150mmDIA

M

M

TM6M

OV3TM

6HBV

2

RED

RED

600X

500

500X

400

TM6M

OV1

TM6G

4

TM6G7TM

6HBV

5

TM6G

6

M

M

TM9MOV3

TM9HBV2

RED

RED

600X500

500X400

TM9MOV1

TM9HBV5

TM9G4

TM9G6

80m

mDIA

M

MTM10MOV3

RED500X400

TM10MOV1

TM10HBV2

TM10G

4TM

10HBV5

TM10G

6

OUT

TM11MOV2

M

M

TM11MOV1

TM11HBV4

TM11G3

TM11G5

TM14

G1

TM14

G2

TM14MOV3

TM14MOV4

M M

TM12MOV1

TM12MOV2

MM

M

M

TM13

HBV5

TM13

MOV4

TM13

MOV6

TM13

G1

TM13

G3

TM13

HBV2

TM15G6

TM15G5

TM15G4

M

M

TM15H

BV2

TM15M

OV1TM

15MOV3

TO FO TANK -9

HB

M

CP M

OV10

M

CP M

OV13300m

mDIA

M

CP M

OV27

TO M

ANIF

OLD

TO H

OLDIA

FROM M

RN P

H

FROM P

UMP H

OUSE

SRN T

O P

UMP H

OUSE

300m

mDIA

MRN A

P G

6FROM S

RN T

ANK 6

MRN A

P G

4

MRN A

P G

2

MRN A

P H

BV 5

MRN A

P G

1

TO P

UMP H

OUSE

400m

mDIA

500m

mDIA

600mm DIA

FROM JE

ETY

(205 )

TO M

ANIF

OLD

TO REFINERY

TO M

ANIF

OLD

CP G

14

(213)

CP M

OV 2

6

M

CP MOV25

500mmDIA

(212 )CP G1

400X300400X300

300Oslash

FROM REFINERY

TO REFINERY

TO REFINERY

TO REFINERY

CP G6(209)

CP G 5(208)

CP G

2

(211)

300m

mDIA

CP M

OV

M

(210)

CP G7HBCP G8

CP MOV17

CPHBV18

MM

(203)(202)CP MOV19

M

CP MOV20(20`)

M

CP MOV21(200)

FROM REFINERY

80Oslash

MRN A

P G

5

PETROCHEMIC

AL L

IMIT

ED

MS

SKO

FO

HSD

MRN

MFMS 5

MFMS4

MFMS 6

P-2

P-1

MRN P

UMP H

OUSE

MAKE- K

IRLOSKER

FLOW

- 277

LPS

HEAD- 1

00M

MOTOR- 3

7KW

1480 R

PM

MAKE- K

IRLOSKER

FLOW

- 283

3LPS

HEAD- 1

00M

MOTOR- 4

5KW

1475 R

PM

PI

PI

PMRN G 1

PMRN G 2

PMRNG3

PMRNG5

PMRNG6

PMRNG4

200m

mDIA

ST-B

S-1

ST-B

S-2

PMRN G 7

200mmDIA

P-2

P-1

SRN P

UMP H

OUSE

MAKE- K

IRLOSKER

FLOW

- 160S

HEAD- 1

00M

MOTOR-9

3KW

1488 R

PM

MAKE- K

IRLOSKER

FLOW

- 160LPS

HEAD- 5

5M

MOTOR- 9

3KW

1488 R

PM

PI

PI

PSRN G

5PSRN G

2

PSRN G3 400m

mDIA

450mmDIA

ST-B

S-1

ST-B

S-2

P-2

P-1

FO P

UMP H

OUSE

MAKE- R

OTO G

EAR

FLOW

- 40 L

PS

HEAD- 1

00M

MOTOR-4

5KW

1480RPM

MAKE- T

ASHACO G

EAR

FLOW

- 80LPS

HEAD- 5

5M

MOTOR- 7

5KW

1450 R

PM

PFG7

PF G

5PFG9

300m

mDIA

200m

mDIA

ST-B

S-1

ST-B

S-2

300mmDIA

200mmDIA

PFG6

PFG8

PFG4

PFG3

100mmDIA

PFG1

PHSG133

PHSG134

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

PHSG129

PHSG128

PHSG127

PHSG126

300mmDIA

400mmDIA

400mmDIA

PHSG125

PHSG4

PHSG4

PHSG2

PHSG1

ST-BS-1

150X200

400X200

NRV

PI

PHSG118

PHSG119

PHSG120

PHSG110

PHSG123

PHSG122

PHSG124

PHSG121

PHSG112

PHSG111

200Oslash

ST-BS-2

400X200

NRV

PI

ST-BS-3

400X200

NRV

P-3ST-BS-4

400X200

400X350

NRV

PI

P-4ST-BS-5

P-5

PI

NRV

PHSG102

80mmDIA

PHSG100

PHSG101

PHSG104

PHSG103

PHSG105

PHSHBV99

PHSG98PHSG97

PHSHBV96

PHSG94PHSG95

PHSG93

PHSG91

PHSG75

PHSG76

PHSHBV81

PHSG82PHSG80

PHSHBV78

PHSG79PHSG77

PHSG85

PHSG85

PHSG85

PHSG87

PHSG90

PHSG84

PHSG83

80mm DIA

PHSG89

200mmDIA

200m

mDIA

PHSHBV40

PHSG39PHSG41

PHSHBV43

PHSG44 PHSG42

400m

mDIA

PHSG46 PHSG45

PHSG48 PHSG47

PHSHBV50

PHSG51PHSG49

PHSHBV53

PHSG52PHSG54

PHSG56

PHSHBV58

PHSG59 PHSG57

PHSG67

PHSG66

PHSHBV61

PHSG62 PHSG60

ST-BS-6

P-6

PI

NRV

400X300

PHSG65 PHSG64

PHSG55

200Oslash

PHSG22

200mmDIA

PHSHBV33

PHSG38 PHSG 37

PHSG35 PHSG 36

PHSG 32PHSG 34

PHSHBV30

PHSG 29 PHSG 31

PHSG 19 PHSG 20

PHSHBV15

PHSG 16 PHSG 14

PHSHBV12

PHSG 11 PHSG 13

PHSHBV9

PHSG 10 PHSG 8

PHSG 18 PHSG 17

PHSG 21

400X200

PHSG 5

PHSHBV27

PHSG26 PHSG28

PHSHBV24

PHSG23PHSG25

PHSG7

PHSG6

P-2 P-1

PHSG69

PHSG68

BAY-5BAY-6BAY-7BAY-8FO

WITHOUTFO

WITHOUTFO

WITHOUT

150mmDIA

FM

FM

200Oslash

TLF BAY

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

BAY-4LSHF HSD

WITH FLOWMETER

amp HOSE

BAY-3LSHF HSD

WITH

BAY-2LSHF HSD

WITH

BAY-1LSHF HSD

WITH FLOWMETER

amp HOSE

FLOWMETER amp HOSE

FLOWMETER amp HOSE

TLF-1

ST-BS-2 ST-BS-1

PTLFG1

PTLFG9

NRV

TLF-3

MAKE- ZALEMITEFLOW- 3333LPSHEAD- 30MMOTOR- 75KW 1440 RPM

ST-BS-3

NRV

FROM TANK 400X200 PTLFG3

SERVICE- LDO

PI

300X200 PTLFG1

300mmDIA

FROM TANK

MAKE-KIRLOSKERFLOW- 3333LPS

MOTOR-15KW1450 RPM

SERVICE- LDO

HEAD- 100M

TLF-2


MOTOR-15KW1450 RPM

SERVICE- LSHF HSD

HEAD- 25 M

PTLFG5

80Oslash

PTLFG6

200X100 PTLFG2

100mmDIA

TO TANK

150m

mDIA

PTLFG8

SKO (OPTIONAL) 400mmDIA

200mmDIA

80mmDIA

PTLFG12

150m

mDIA

PI PI

200mmDIA

200X150

PTLFG14

TLF PUMP HOUSE

150m

mDIA

LSHS HSD

FO

100mmDIA

mas

MFHSDG2

MFHSDG1

MP H

SD 9

(281)

(282)

(280)

(277)

(278)

MF H

SD 7

5

300m

mDI A

400mmDIA

P-2

P-1

MS P

UMP H

OUSE

MAKE- K

I RLOSKER

FLOW

- 160S

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

MAKE- K

I RLOSKER

FLOW

- 160LPS

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

200m

mDIA

ST-B

S-1

ST-B

S-2 300Oslash

300mmDIA

PMG8

PMG9

PMG10

PMG11

300X200

300X200

NRV

PMG7

PMG3

PMG4

PMG5

PMG6

NRV

300X200

PMG2

300X200

300mmDIA

TO H

B

TO H

MR

PMG13

PMG 1

4

PMG 1

5

PMG 1

6

PM M

OV 1

M

HSD

HSD

300m

mDIA

SKO

M M MCPMOV30(1

86)

CPMOV29(1

85)

CPMOV28(1

84)

800X300

800X500

800X500

M M MCPMOV31(1

83)

CPMOV32(1

82)

CPMOV33(1

81)

SB

SB

SB

SB

SB

SB

SB

SB

MCPMOV40(1

95)

HSDTO M10M11

HSDTO M8

M

CPMOV38(1

76)

300mmDIA

MMSB

CPMOV51

CPMOV52

80m

mDIA

DRAIN

SB

SB

MCPMOV49

MCPMOV48

MCPMOV46

M

MCPMOV47

MCPMOV43

SB

SB

SB

SB

SB

SB

M CPMOV41

SKO TO M7MCPMOV42

200mmDIA

200mmDIA

PSRN G4

DETAIL

OF P

UMPS( T

RANSFER P

UMP H

OUSE)

P-1

HSD B

URGE L

OADIN

G P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-2

SKO H

B P

IPE L

INE

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0M

MOTOR--6

7KW

1470 R

PM

BOOSTER P

UMP

MAKE--C

GL

MAKE--C

GL

HSD H

B P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-3

P-4

SKO H

MR B

OOSTER P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--1

60 L

PS

HEAD--5

5 M

MOTOR--1

10KW

1485 R

PM

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-5

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-6

FROM R

EFIN

ARY

100mmDIA

300m

mDIA

LOAD A

RAM

LOAD A

RAM

LOAD A

RAM

FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

mDIA

500m

mDIA

300m

mDIA

300mmDIA

300mmDIA

700m

mDIA

700m

mDIA

MM

CPMOV36(1

74)

CPMOV37(1

75)

80m

mDIA

DRAIN

80m

mDIA

DRAIN

80m

mDIA

DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

PTLFG15

PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

PHSG135

PHSG135

FROM T

ANK

200X80400m

mDIA

PHSG120

PHSG116

PHSG117

TO

PMG 1

2

300m

mDIA

300m

mDIA

PMG 1

8PMG17

JETTY-1

PHSG72

200mmDIA

PHSG74

PHSG73

PHSG63

PHSG92

PHSG116

PHSHB114

PHSG109

PHSG117

PHSHB113

PMG 1

2

PHSG63

300m

mDIA

200m

mDIA

700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

mDI A

300mmDIA

300m

mDIA

150m

mDIA

NRV

150m

mDIA

400mmDIA

150m

mDIA

150m

mDIA

80mmDIA

200mmDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II



451 Additional facilities at Haldia refinery will involve engineering and execution of a new common 18 inch discharge header for hooking up with the existing booster pump discharges from refinery tanks and laying of this pipeline up to HBPL boosters

452 Additional marketing facilities at Haldia Jasidih will involve modification to existing pipes valves amp flanges etc to accommodate higher flow rate

452 Engineering and execution of the above facilities will be carried out by respective Divisions Estimated cost towards these additional facilities has been incorporated in the capital cost

46 Pipeline Route

461 Pipeline will originate from PHBPL pump station at Haldia The new pipeline would be laid in common RoW of PHBPL up to Bolpur station (ch 206 km) from Haldia Thereafter it will travel in new RoW via Jasidih from ch 206 km to ch 465 km Subs

462 The proposed Haldia-Barauni product pipeline traverses through 5 districts of West Bengal covering a length of 267 km and 2 district in Jharkhand covering a length 120 km and also traverses through 5 districts of Bihar covering length of 148

463 The terrain along the pipeline route is mostly flat and rolling The agricultural crop grows in the region are mostly Paddy

464 The proposed Haldia-Barauni pipeline will not pass through any ReservedProtected forest all along the route Although reserve forest has been avoided in fixing the pipeline alignment village forests and forest in Government land along the prop

47 Civil



491 Mechanical

410 Electrical


41011 Power supply of 66 kV shall be made available from Haldia Ref HMR New HT Panel has been envisaged for new Booster motors with Soft Starter Panels Presently power supply is coming from State Electricity Board at HMR Haldia Accordingly

41012 LT Power supply for new facilities shall be arranged from HMR Haldia and new LT Panel has been envisaged


41014 Electrical power of approx 800 KVA for BPMOVLightingMainline CP etc shall be provided by existing incoming Power supply 66kV0415kV through existing HMR Haldia Haldia Refinery


41021 66 kV Power supply shall be made available from PHBPL Haldia switchyard under PHDPL Project with addition of 1 additional 125MVA Bay

41022 LT Power supply for new facilities shall be arranged from new 660415kV 500KVA Transformer at Haldia and new LT Panel has been envisaged


41024 Electrical power of approx 2400 KVA for MLPUMOVLightingMainline CP etc shall be provided by existing incoming Power supply 33kV from WBSEDCL through 3366kV 125MVA Switchyard at Haldia by means of an additional bay at Haldia New Tr

4103 Bolpur Station

41031 Existing Contract demand is 400KVA at 11kV Supply Voltage additional load requirement of 100 kVA shall be made from existing supply

41032 LT Power supply for new facilities shall be arranged from SEB and new LT Panel has been envisaged LT DG set 415V 500KVA has been envisaged



41041 Mains power supply of 40KVA at 415V voltage level shall be arranged from existing Marketing TerminalPL Terminal at Jasidih

41042 LT Power supply for new facilities shall be arranged from Jasidih and new LT Panel has been envisaged LT DG set has been envisaged

41043 Facilities like MOVrsquos LT MCC Panel High Mast etc are required and have been considered

41044 Electrical power of approx 40 KVA for MOVLightingMainline CP etc shall be provided by existing incoming Power supply 415V from Pipeline facilities through Marketing terminal at Jasidih


41051 Mains power supply of 80 kVA at 415V voltage level shall be arranged from existing Marketing TerminalPL Terminal at Barauni

41052 LT Power supply for new facilities shall be arranged from Barauni and new LT Panel has been envisaged LT DG set 415V 100KVA has been envisaged


41054 Electrical power of approx 80 KVA for MOVLightingMainline CP etc shall be required which shall be provided by existing incoming Power supply 415V from Marketing terminal at Barauni


4111 At Bolpur three motor-driven mainline pumping units (2 operating + 1 stand by) having variable frequency drive (VFD) along with 12rdquo delivery manifold a skid mounted OWS of 10klhr capacity and 12rdquo fire water hydrant network has been considere

4112 3366kV 10MVA Switchyard is required for catering to power supply from SEB HT DG set of 66 kV 2 MVA has been envisaged


4121 Instrumentation will be provided to cater for operation and control to optimise the use of equipment and manpower and to protect the equipment All stations will be provided with hot standby PLC based station control system (except block valve

4122 The field instrumentation at station comprises of pressure transmitter pressure switches pressure gauges mass flow meters Ultrasonic flow meters flow switches level switches level transmitters density meters temperature transmitter sc

4123 Mass Flow Meters have been considered at originating and delivery stations and ultrasonic flow meters have been considered at Intermediate pump stations

4124 Station Control Centre (SCC) shall have Workstations system as operator interface to the station instrumentation and control system The computers shall be connected to dual local area networking (LAN) in client server mode They shall work in

4125 Jasidih is an existing delivery station where scrapper facilities and hook up with existing delivery facilities are proposed under the project The existing control system of Jasidih will continue to be in use and will be hooked up with the ne

4126 The system power supply shall be through UPS system with battery backup for round the clock uninterrupted operation

4127 The Station Control Centrersquos shall be connected to the Master Control Stations through LAN and WAN for SCADA operation


4131 A dedicated state of the art OFC based STM-16 25 Gbps SDH (Synchronous Digital Hierarchy) communication system with 999 availability is envisaged SDH is a standard technology for synchronous data transmission on optical media (Optical Fibre

Out of total 535 km of mainline new OFC shall be laid for approx 472 km and for balance ie in Khana-Bolpur amp Dumri-Barauni sections the OFC being laid under the PHBPL- Aug project will be utilised for the communications

4132 For the entire communication network of the pipeline the following type of stations have been considered -


RCP Stations 3 Nos

SV locations 37 Nos

4133 RTU data amp CCTV requirements of SV locations considered all along the pipeline shall be catered by the network connectivity using fibre of the OFC network

4134 The NMS (Network Management System) for the SDH network is planned at Haldia to monitor amp configure the telecom network hardware from centralised location

4135 It is proposed to install IP amp E1 based new EPABX Systems at all manned locations to provide dedicated voice communications for operations

4136 The power requirement of equipment shall be met with the power systems (Battery charger + battery bank) at all manned locations At RCP locations amp SV locations dedicated battery chargers with battery bank + Solar System have been considered

4137 CCTV based Surveillance system has been considered for all manned stations as well as RCPSV locations

4138 Control Centre for CCTV System has been envisaged at Haldia for monitoring amp recording of CCTV cameras for whole pipeline section This feed shall be available over LAN at all stations on Ethernet

4139 VHF System (Base Station + 8 nos hand held sets for originating pumping stations and 6 nos hand held sets for delivery stations) have been considered for all manned locations

41310 No Telecom equipment (except network switches telephone instruments VHF sets) has been considered at Booster station inside Haldia Refinery Only OFC laying (approx 7 km) has been considered for SCADA connectivity which shall be achieved on


4141 The Tele-supervisory system for the proposed pipeline is envisaged to have dual hot stand-by computer system in client-server mode sitting on dual local area network (LAN) for round the clock monitoring and control of pipeline from a centralise

4142 RTU has been considered for all RCP amp Block valve locations to control amp monitor the local facilities from remote centralized master location

4143 It is envisaged to have Master Control Station at Haldia Station The Master Control Station shall be equipped with Supervisory Control and Data Acquisition (SCADA) software running under multi-programming multi-tasking real time operating sys

4144 Leak Detection system has been envisaged for complete section of the Pipeline Leak Detection Software shall run in a separate machine at Master Control Station This package will enable the operator to take optimal control actions and thus ens


4151 Safety PLC based fire amp gas detection system along with hydrocarbon detectors amp UVIR Flame detectors have been envisaged at all attended stations (including booster station inside Haldia premises)

4152 Fire Alarm Panel along with multi-sensor amp heat detectors have been considered at attended stations At Block Valve locations hydro carbon detectors multi-sensor detectors etc have been considered as per requirement

4153 FM200 based Fire extinguishing systems have been considered for Control rooms of all attended stations

4154 CO2 based (which will be reviewed during detailed engineering stage) Fire extinguishing systems have been considered for HT VFD buildings and Equipment rooms of all attended stations



4171 Minimum batch length for MS and HSD has been worked out considering simultaneous delivery at Jasidih and Barauni Considering absorption of 1 SKO in MS and 1 SKO in HSD minimum batch length required is 30000 kl and 33000 kl for MS and HSD re

4172 In case of non-availability of MSHSD batch as above or due to unplanned shutdown of the pipeline interface might increase in the pipeline and some unabsorbed interface may be there which would be delivered in the transmix tanks at Barauni MS

4173 Tankages

41731 LBT-04 of gross capacity of 3500 kl which is a FR tank at Barauni being used in HSD service will be changed to MS for pipeline operation



419 Condemnation

4191 The existing 1275OD pipeline would continue to remain in use till completion of proposed scheme

4192 Upon successful commissioning of new pipeline action would be initiated for condemnation of existing pipeline

4193 The existing intermediate pumping station at Asansol would be redundant and would be decommissioned Mainline pumping units at Haldia amp Asansol would be suitably utilized at some other pipeline location as per requirement



CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1




Contents

Chapter No

Description Page No

Executive Summary [i] - [xi]

I Introduction 2

II Need and Justification 4

III Design Philosophy 10

IV Project Description 11

V Safety Health amp Environment 25

VI Capital Costs 31

VII Operating Costs 34

VIII Financial Analysis 36

IX Conclusions amp Recommendations 38

Annexures

A Hydraulic Gradient Annexure-I

B System Configuration Annexure-II

C Indicative Route Annexure-III

D Completion Schedule Annexure-IV

E Capital Cost Annexure-V

F Operating Cost Annexure-VI

Appendix-i (Highlights of Geophysical Survey)

Appendix-ii (Optimization Study Report)

EXECUTIVE SUMMARY




EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION

















































Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121




















































216 Design Capacity












216 Design Capacity












216 Design Capacity













Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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FM FM FM

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500mm DIA

300mm DIA

300mm DIA

500m

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500m

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300m

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300mmDIA

300mmDIA

700m

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700m

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80m

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400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

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PHSG132

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300m

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200m

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700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

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300mmDIA

300m

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150m

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150m

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400mmDIA

150m

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150m

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80mmDIA

200mmDIA

400m

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400m

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400m

mDIA

400m

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400m

mDIA

400m

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400m

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Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1

EXECUTIVE SUMMARY




EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION

















































Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121




















































216 Design Capacity












216 Design Capacity












216 Design Capacity













Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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200mmDIA

200m

mDIA

PHSHBV40

PHSG39PHSG41

PHSHBV43

PHSG44 PHSG42

400m

mDIA

PHSG46 PHSG45

PHSG48 PHSG47

PHSHBV50

PHSG51PHSG49

PHSHBV53

PHSG52PHSG54

PHSG56

PHSHBV58

PHSG59 PHSG57

PHSG67

PHSG66

PHSHBV61

PHSG62 PHSG60

ST-BS-6

P-6

PI

NRV

400X300

PHSG65 PHSG64

PHSG55

200Oslash

PHSG22

200mmDIA

PHSHBV33

PHSG38 PHSG 37

PHSG35 PHSG 36

PHSG 32PHSG 34

PHSHBV30

PHSG 29 PHSG 31

PHSG 19 PHSG 20

PHSHBV15

PHSG 16 PHSG 14

PHSHBV12

PHSG 11 PHSG 13

PHSHBV9

PHSG 10 PHSG 8

PHSG 18 PHSG 17

PHSG 21

400X200

PHSG 5

PHSHBV27

PHSG26 PHSG28

PHSHBV24

PHSG23PHSG25

PHSG7

PHSG6

P-2 P-1

PHSG69

PHSG68


WITHOUTFO

WITHOUTFO

WITHOUT

150mmDIA

FM

FM

200Oslash

TLF BAY

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

BAY-4LSHF HSD

WITH FLOWMETER

amp HOSE

BAY-3LSHF HSD

WITH

BAY-2LSHF HSD

WITH

BAY-1LSHF HSD

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amp HOSE

FLOWMETER amp HOSE

FLOWMETER amp HOSE

TLF-1

ST-BS-2 ST-BS-1

PTLFG1

PTLFG9

NRV

TLF-3


ST-BS-3

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SERVICE- LDO

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300X200 PTLFG1

300mmDIA

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80Oslash

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100mmDIA

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150m

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200mmDIA

80mmDIA

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150m

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200mmDIA

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ST-B

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300mmDIA

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PMG9

PMG10

PMG11

300X200

300X200

NRV

PMG7

PMG3

PMG4

PMG5

PMG6

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B

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PMG 1

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CPMOV29(1

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CPMOV32(1

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CPMOV33(1

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MCPMOV40(1

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HSDTO M10M11

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M

CPMOV38(1

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300mmDIA

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CPMOV51

CPMOV52

80m

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DRAIN

SB

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MCPMOV49

MCPMOV48

MCPMOV46

M

MCPMOV47

MCPMOV43

SB

SB

SB

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SB

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M CPMOV41

SKO TO M7MCPMOV42

200mmDIA

200mmDIA

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DETAIL

OF P

UMPS( T

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100mmDIA

300m

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LOAD A

RAM

LOAD A

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LOAD A

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FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

mDIA

500m

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300m

mDIA

300mmDIA

300mmDIA

700m

mDIA

700m

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MM

CPMOV36(1

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CPMOV37(1

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80m

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DRAIN

80m

mDIA

DRAIN

80m

mDIA

DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

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PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

PHSG135

PHSG135

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PHSG117

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300m

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300m

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JETTY-1

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200mmDIA

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PHSG73

PHSG63

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300m

mDIA

200m

mDIA

700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

mDI A

300mmDIA

300m

mDIA

150m

mDIA

NRV

150m

mDIA

400mmDIA

150m

mDIA

150m

mDIA

80mmDIA

200mmDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1




EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION












EXECUTIVE SUMMARY

10 INTRODUCTION

















































Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121




















































216 Design Capacity












216 Design Capacity












216 Design Capacity













Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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100mmDIA

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PHSG134

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

PHSG129

PHSG128

PHSG127

PHSG126

300mmDIA

400mmDIA

400mmDIA

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PHSG98PHSG97

PHSHBV96

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PHSG93

PHSG91

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200mmDIA

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PHSG48 PHSG47

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PHSG 32PHSG 34

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PHSG 29 PHSG 31

PHSG 19 PHSG 20

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200mmDIA

300mmDIA

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100m

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150m

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300mmDIA

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150m

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Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1









































Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121








Fig in MMTPA



Assumptions


Findings




2012-13 1252013-14 1012014-15 121




















































216 Design Capacity












216 Design Capacity












216 Design Capacity













Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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14

CAP- 1

4143 K

L

38M D

IA X

13M H

T

MS

CLASS-A

CAP- 5

430 K

L

MS

TANK N

O- M

15

CLASS-A

FR T

ANK

LT

24M D

IA X

13M H

T

DEEP T

UBE

WELL

CAP- 1

4143 K

L

TANK N

O- M

11

38M D

IA X

13 M

HT

CLASS-B

BS-II

HSD

CR T

ANK

HNG

SLOP

IN

HSD

6000 WIDE ROAD

HSD (L

SHF)

SKO

TANK N

O- M

4

CLASS-B

CR T

ANK

CAP- 1

0207 K

L

38M D

IA X

96

M H

T

LDO

TANK N

O- M

1

CLASS-C

CR T

ANK

CAP- 4

684 K

L

26M D

IA X

92

MHT

50M D

IA X

112

6M H

T

CAP- 1

8650 K

L

SEPARATOR

OIL

WATER

PUMP HOUSE

TANK N

O- M

6

SRN

FR T

ANK

CLASS-A

CR T

ANK

TANK N

O- M

5

38M D

IA X

99

M H

T

CAP- 1

0207 K

L

CLASS-C

IN

MANIF

OLD-2

DELIV

ERY

6

50M D

IA X

114

M H

T

CAP- 2

1576 K

L

TANK N

O- M

8

8000 W

IDE R

OAD

MANIF

OLD

3000 X

2000

SECURIT

Y R

OOM

HSD

BS-II

OUT

INRECEIP

T

55M D

IA X

13M H

T

TANK N

O- M

10

CAP- 2

9755 K

L

CR T

ANK

CLASS-B

8000 W

IDE ROAD

50M D

IA X

114

M H

T

CAP- 2

1576 K

L

6000 WIDE ROAD

SKO

TANK N

O- M

7

OUT

IN

ENCLOSURE W

ALL

CLASS-B

CR T

ANK

LT

SLOP R

ECOVERY

PUMP H

OUSE

3000 X

5000

6000 WIDE RO

AD

HSD

CR T

ANK

CLASS-B

OIL

WATER

SEPARATOR

6000 W

IDE ROAD

FO

FIRE BREAK WALL

IN

IN

OUT

FO

6000 WIDE RO

AD

CAP- 7

722 K

L

FO

CLASS-C

CR T

ANK

TANK N

O- M

9

30M D

IA X

114

M H

T

6000 W

IDE R

OAD

M TM2HBV2

M

TM2M

OV3TM2M

OV1

TM2G4

TM2HBV5

TM2G6

OUT

TM3G

4

TM3H

BV5

TM3G

3

TM3HBV2

TM3M

OV3TM3M

OV1

M

M

TM1G1

TM1G4

TM1G5

TM1HBV2

TM1G3

300mmDIA

80mmDIA

80mmDIA

150mmDIA

MM

TM4H

BV2

TM4M

OV3

TM4M

OV1

TM3G

6TM

3HBV

5TM

3G4

MM

TM5H

BV2

TM5M

OV3

TM5M

OV1

TM5G6

TM5HBV5

TM5G4

80mmDIA

150mmDIA

M

MTM7MOV3

TM7HBV2

RED

RED600X500500X400

TM7MOV1

TM7G

6

TM7G

4

TM7G7

TM7H

BV5

40mmDIA

M

MTM8MOV3

TM8HBV2

RED

RED

600X500

500X400

TM8MOV1

TM8G6 TM8G4

TM8HBV5

40mmDIA

150mmDIA

M

M

TM6M

OV3TM

6HBV

2

RED

RED

600X

500

500X

400

TM6M

OV1

TM6G

4

TM6G7TM

6HBV

5

TM6G

6

M

M

TM9MOV3

TM9HBV2

RED

RED

600X500

500X400

TM9MOV1

TM9HBV5

TM9G4

TM9G6

80m

mDIA

M

MTM10MOV3

RED500X400

TM10MOV1

TM10HBV2

TM10G

4TM

10HBV5

TM10G

6

OUT

TM11MOV2

M

M

TM11MOV1

TM11HBV4

TM11G3

TM11G5

TM14

G1

TM14

G2

TM14MOV3

TM14MOV4

M M

TM12MOV1

TM12MOV2

MM

M

M

TM13

HBV5

TM13

MOV4

TM13

MOV6

TM13

G1

TM13

G3

TM13

HBV2

TM15G6

TM15G5

TM15G4

M

M

TM15H

BV2

TM15M

OV1TM

15MOV3

TO FO TANK -9

HB

M

CP M

OV10

M

CP M

OV13300m

mDIA

M

CP M

OV27

TO M

ANIF

OLD

TO H

OLDIA

FROM M

RN P

H

FROM P

UMP H

OUSE

SRN T

O P

UMP H

OUSE

300m

mDIA

MRN A

P G

6FROM S

RN T

ANK 6

MRN A

P G

4

MRN A

P G

2

MRN A

P H

BV 5

MRN A

P G

1

TO P

UMP H

OUSE

400m

mDIA

500m

mDIA

600mm DIA

FROM JE

ETY

(205 )

TO M

ANIF

OLD

TO REFINERY

TO M

ANIF

OLD

CP G

14

(213)

CP M

OV 2

6

M

CP MOV25

500mmDIA

(212 )CP G1

400X300400X300

300Oslash

FROM REFINERY

TO REFINERY

TO REFINERY

TO REFINERY

CP G6(209)

CP G 5(208)

CP G

2

(211)

300m

mDIA

CP M

OV

M

(210)

CP G7HBCP G8

CP MOV17

CPHBV18

MM

(203)(202)CP MOV19

M

CP MOV20(20`)

M

CP MOV21(200)

FROM REFINERY

80Oslash

MRN A

P G

5

PETROCHEMIC

AL L

IMIT

ED

MS

SKO

FO

HSD

MRN

MFMS 5

MFMS4

MFMS 6

P-2

P-1

MRN P

UMP H

OUSE

MAKE- K

IRLOSKER

FLOW

- 277

LPS

HEAD- 1

00M

MOTOR- 3

7KW

1480 R

PM

MAKE- K

IRLOSKER

FLOW

- 283

3LPS

HEAD- 1

00M

MOTOR- 4

5KW

1475 R

PM

PI

PI

PMRN G 1

PMRN G 2

PMRNG3

PMRNG5

PMRNG6

PMRNG4

200m

mDIA

ST-B

S-1

ST-B

S-2

PMRN G 7

200mmDIA

P-2

P-1

SRN P

UMP H

OUSE

MAKE- K

IRLOSKER

FLOW

- 160S

HEAD- 1

00M

MOTOR-9

3KW

1488 R

PM

MAKE- K

IRLOSKER

FLOW

- 160LPS

HEAD- 5

5M

MOTOR- 9

3KW

1488 R

PM

PI

PI

PSRN G

5PSRN G

2

PSRN G3 400m

mDIA

450mmDIA

ST-B

S-1

ST-B

S-2

P-2

P-1

FO P

UMP H

OUSE

MAKE- R

OTO G

EAR

FLOW

- 40 L

PS

HEAD- 1

00M

MOTOR-4

5KW

1480RPM

MAKE- T

ASHACO G

EAR

FLOW

- 80LPS

HEAD- 5

5M

MOTOR- 7

5KW

1450 R

PM

PFG7

PF G

5PFG9

300m

mDIA

200m

mDIA

ST-B

S-1

ST-B

S-2

300mmDIA

200mmDIA

PFG6

PFG8

PFG4

PFG3

100mmDIA

PFG1

PHSG133

PHSG134

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

PHSG129

PHSG128

PHSG127

PHSG126

300mmDIA

400mmDIA

400mmDIA

PHSG125

PHSG4

PHSG4

PHSG2

PHSG1

ST-BS-1

150X200

400X200

NRV

PI

PHSG118

PHSG119

PHSG120

PHSG110

PHSG123

PHSG122

PHSG124

PHSG121

PHSG112

PHSG111

200Oslash

ST-BS-2

400X200

NRV

PI

ST-BS-3

400X200

NRV

P-3ST-BS-4

400X200

400X350

NRV

PI

P-4ST-BS-5

P-5

PI

NRV

PHSG102

80mmDIA

PHSG100

PHSG101

PHSG104

PHSG103

PHSG105

PHSHBV99

PHSG98PHSG97

PHSHBV96

PHSG94PHSG95

PHSG93

PHSG91

PHSG75

PHSG76

PHSHBV81

PHSG82PHSG80

PHSHBV78

PHSG79PHSG77

PHSG85

PHSG85

PHSG85

PHSG87

PHSG90

PHSG84

PHSG83

80mm DIA

PHSG89

200mmDIA

200m

mDIA

PHSHBV40

PHSG39PHSG41

PHSHBV43

PHSG44 PHSG42

400m

mDIA

PHSG46 PHSG45

PHSG48 PHSG47

PHSHBV50

PHSG51PHSG49

PHSHBV53

PHSG52PHSG54

PHSG56

PHSHBV58

PHSG59 PHSG57

PHSG67

PHSG66

PHSHBV61

PHSG62 PHSG60

ST-BS-6

P-6

PI

NRV

400X300

PHSG65 PHSG64

PHSG55

200Oslash

PHSG22

200mmDIA

PHSHBV33

PHSG38 PHSG 37

PHSG35 PHSG 36

PHSG 32PHSG 34

PHSHBV30

PHSG 29 PHSG 31

PHSG 19 PHSG 20

PHSHBV15

PHSG 16 PHSG 14

PHSHBV12

PHSG 11 PHSG 13

PHSHBV9

PHSG 10 PHSG 8

PHSG 18 PHSG 17

PHSG 21

400X200

PHSG 5

PHSHBV27

PHSG26 PHSG28

PHSHBV24

PHSG23PHSG25

PHSG7

PHSG6

P-2 P-1

PHSG69

PHSG68


WITHOUTFO

WITHOUTFO

WITHOUT

150mmDIA

FM

FM

200Oslash

TLF BAY

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

BAY-4LSHF HSD

WITH FLOWMETER

amp HOSE

BAY-3LSHF HSD

WITH

BAY-2LSHF HSD

WITH

BAY-1LSHF HSD

WITH FLOWMETER

amp HOSE

FLOWMETER amp HOSE

FLOWMETER amp HOSE

TLF-1

ST-BS-2 ST-BS-1

PTLFG1

PTLFG9

NRV

TLF-3


ST-BS-3

NRV


SERVICE- LDO

PI

300X200 PTLFG1

300mmDIA

FROM TANK


MOTOR-15KW1450 RPM

SERVICE- LDO

HEAD- 100M

TLF-2


MOTOR-15KW1450 RPM

SERVICE- LSHF HSD

HEAD- 25 M

PTLFG5

80Oslash

PTLFG6

200X100 PTLFG2

100mmDIA

TO TANK

150m

mDIA

PTLFG8


200mmDIA

80mmDIA

PTLFG12

150m

mDIA

PI PI

200mmDIA

200X150

PTLFG14

TLF PUMP HOUSE

150m

mDIA

LSHS HSD

FO

100mmDIA

mas

MFHSDG2

MFHSDG1

MP H

SD 9

(281)

(282)

(280)

(277)

(278)

MF H

SD 7

5

300m

mDI A

400mmDIA

P-2

P-1

MS P

UMP H

OUSE

MAKE- K

I RLOSKER

FLOW

- 160S

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

MAKE- K

I RLOSKER

FLOW

- 160LPS

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

200m

mDIA

ST-B

S-1

ST-B

S-2 300Oslash

300mmDIA

PMG8

PMG9

PMG10

PMG11

300X200

300X200

NRV

PMG7

PMG3

PMG4

PMG5

PMG6

NRV

300X200

PMG2

300X200

300mmDIA

TO H

B

TO H

MR

PMG13

PMG 1

4

PMG 1

5

PMG 1

6

PM M

OV 1

M

HSD

HSD

300m

mDIA

SKO

M M MCPMOV30(1

86)

CPMOV29(1

85)

CPMOV28(1

84)

800X300

800X500

800X500

M M MCPMOV31(1

83)

CPMOV32(1

82)

CPMOV33(1

81)

SB

SB

SB

SB

SB

SB

SB

SB

MCPMOV40(1

95)

HSDTO M10M11

HSDTO M8

M

CPMOV38(1

76)

300mmDIA

MMSB

CPMOV51

CPMOV52

80m

mDIA

DRAIN

SB

SB

MCPMOV49

MCPMOV48

MCPMOV46

M

MCPMOV47

MCPMOV43

SB

SB

SB

SB

SB

SB

M CPMOV41

SKO TO M7MCPMOV42

200mmDIA

200mmDIA

PSRN G4

DETAIL

OF P

UMPS( T

RANSFER P

UMP H

OUSE)

P-1

HSD B

URGE L

OADIN

G P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-2

SKO H

B P

IPE L

INE

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0M

MOTOR--6

7KW

1470 R

PM

BOOSTER P

UMP

MAKE--C

GL

MAKE--C

GL

HSD H

B P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-3

P-4

SKO H

MR B

OOSTER P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--1

60 L

PS

HEAD--5

5 M

MOTOR--1

10KW

1485 R

PM

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-5

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-6

FROM R

EFIN

ARY

100mmDIA

300m

mDIA

LOAD A

RAM

LOAD A

RAM

LOAD A

RAM

FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

mDIA

500m

mDIA

300m

mDIA

300mmDIA

300mmDIA

700m

mDIA

700m

mDIA

MM

CPMOV36(1

74)

CPMOV37(1

75)

80m

mDIA

DRAIN

80m

mDIA

DRAIN

80m

mDIA

DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

PTLFG15

PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

PHSG135

PHSG135

FROM T

ANK

200X80400m

mDIA

PHSG120

PHSG116

PHSG117

TO

PMG 1

2

300m

mDIA

300m

mDIA

PMG 1

8PMG17

JETTY-1

PHSG72

200mmDIA

PHSG74

PHSG73

PHSG63

PHSG92

PHSG116

PHSHB114

PHSG109

PHSG117

PHSHB113

PMG 1

2

PHSG63

300m

mDIA

200m

mDIA

700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

mDI A

300mmDIA

300m

mDIA

150m

mDIA

NRV

150m

mDIA

400mmDIA

150m

mDIA

150m

mDIA

80mmDIA

200mmDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1




















































216 Design Capacity












216 Design Capacity












216 Design Capacity













Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








13

13

13

13

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6000 W

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CAP- 1

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24M D

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26M D

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TANK N

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TM2HBV5

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TM3H

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TM3G

3

TM3HBV2

TM3M

OV3TM3M

OV1

M

M

TM1G1

TM1G4

TM1G5

TM1HBV2

TM1G3

300mmDIA

80mmDIA

80mmDIA

150mmDIA

MM

TM4H

BV2

TM4M

OV3

TM4M

OV1

TM3G

6TM

3HBV

5TM

3G4

MM

TM5H

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TM5M

OV3

TM5M

OV1

TM5G6

TM5HBV5

TM5G4

80mmDIA

150mmDIA

M

MTM7MOV3

TM7HBV2

RED

RED600X500500X400

TM7MOV1

TM7G

6

TM7G

4

TM7G7

TM7H

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40mmDIA

M

MTM8MOV3

TM8HBV2

RED

RED

600X500

500X400

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TM8G6 TM8G4

TM8HBV5

40mmDIA

150mmDIA

M

M

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OV3TM

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RED

600X

500

500X

400

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TM6G

4

TM6G7TM

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5

TM6G

6

M

M

TM9MOV3

TM9HBV2

RED

RED

600X500

500X400

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TM9HBV5

TM9G4

TM9G6

80m

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M

MTM10MOV3

RED500X400

TM10MOV1

TM10HBV2

TM10G

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10HBV5

TM10G

6

OUT

TM11MOV2

M

M

TM11MOV1

TM11HBV4

TM11G3

TM11G5

TM14

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TM14

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TM14MOV3

TM14MOV4

M M

TM12MOV1

TM12MOV2

MM

M

M

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HBV5

TM13

MOV4

TM13

MOV6

TM13

G1

TM13

G3

TM13

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TM15G6

TM15G5

TM15G4

M

M

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TO FO TANK -9

HB

M

CP M

OV10

M

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M

CP M

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P G

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4

MRN A

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2

MRN A

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500m

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600mm DIA

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TO REFINERY

TO REFINERY

CP G6(209)

CP G 5(208)

CP G

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M

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CP G7HBCP G8

CP MOV17

CPHBV18

MM

(203)(202)CP MOV19

M

CP MOV20(20`)

M

CP MOV21(200)

FROM REFINERY

80Oslash

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- 283

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5KW

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PI

PI

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PMRN G 2

PMRNG3

PMRNG5

PMRNG6

PMRNG4

200m

mDIA

ST-B

S-1

ST-B

S-2

PMRN G 7

200mmDIA

P-2

P-1

SRN P

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OUSE

MAKE- K

IRLOSKER

FLOW

- 160S

HEAD- 1

00M

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1488 R

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MAKE- K

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HEAD- 5

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PM

PI

PI

PSRN G

5PSRN G

2

PSRN G3 400m

mDIA

450mmDIA

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S-1

ST-B

S-2

P-2

P-1

FO P

UMP H

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MAKE- R

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EAR

FLOW

- 40 L

PS

HEAD- 1

00M

MOTOR-4

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MAKE- T

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FLOW

- 80LPS

HEAD- 5

5M

MOTOR- 7

5KW

1450 R

PM

PFG7

PF G

5PFG9

300m

mDIA

200m

mDIA

ST-B

S-1

ST-B

S-2

300mmDIA

200mmDIA

PFG6

PFG8

PFG4

PFG3

100mmDIA

PFG1

PHSG133

PHSG134

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

PHSG129

PHSG128

PHSG127

PHSG126

300mmDIA

400mmDIA

400mmDIA

PHSG125

PHSG4

PHSG4

PHSG2

PHSG1

ST-BS-1

150X200

400X200

NRV

PI

PHSG118

PHSG119

PHSG120

PHSG110

PHSG123

PHSG122

PHSG124

PHSG121

PHSG112

PHSG111

200Oslash

ST-BS-2

400X200

NRV

PI

ST-BS-3

400X200

NRV

P-3ST-BS-4

400X200

400X350

NRV

PI

P-4ST-BS-5

P-5

PI

NRV

PHSG102

80mmDIA

PHSG100

PHSG101

PHSG104

PHSG103

PHSG105

PHSHBV99

PHSG98PHSG97

PHSHBV96

PHSG94PHSG95

PHSG93

PHSG91

PHSG75

PHSG76

PHSHBV81

PHSG82PHSG80

PHSHBV78

PHSG79PHSG77

PHSG85

PHSG85

PHSG85

PHSG87

PHSG90

PHSG84

PHSG83

80mm DIA

PHSG89

200mmDIA

200m

mDIA

PHSHBV40

PHSG39PHSG41

PHSHBV43

PHSG44 PHSG42

400m

mDIA

PHSG46 PHSG45

PHSG48 PHSG47

PHSHBV50

PHSG51PHSG49

PHSHBV53

PHSG52PHSG54

PHSG56

PHSHBV58

PHSG59 PHSG57

PHSG67

PHSG66

PHSHBV61

PHSG62 PHSG60

ST-BS-6

P-6

PI

NRV

400X300

PHSG65 PHSG64

PHSG55

200Oslash

PHSG22

200mmDIA

PHSHBV33

PHSG38 PHSG 37

PHSG35 PHSG 36

PHSG 32PHSG 34

PHSHBV30

PHSG 29 PHSG 31

PHSG 19 PHSG 20

PHSHBV15

PHSG 16 PHSG 14

PHSHBV12

PHSG 11 PHSG 13

PHSHBV9

PHSG 10 PHSG 8

PHSG 18 PHSG 17

PHSG 21

400X200

PHSG 5

PHSHBV27

PHSG26 PHSG28

PHSHBV24

PHSG23PHSG25

PHSG7

PHSG6

P-2 P-1

PHSG69

PHSG68


WITHOUTFO

WITHOUTFO

WITHOUT

150mmDIA

FM

FM

200Oslash

TLF BAY

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

FLOWMETER

amp HOSE

BAY-4LSHF HSD

WITH FLOWMETER

amp HOSE

BAY-3LSHF HSD

WITH

BAY-2LSHF HSD

WITH

BAY-1LSHF HSD

WITH FLOWMETER

amp HOSE

FLOWMETER amp HOSE

FLOWMETER amp HOSE

TLF-1

ST-BS-2 ST-BS-1

PTLFG1

PTLFG9

NRV

TLF-3


ST-BS-3

NRV


SERVICE- LDO

PI

300X200 PTLFG1

300mmDIA

FROM TANK


MOTOR-15KW1450 RPM

SERVICE- LDO

HEAD- 100M

TLF-2


MOTOR-15KW1450 RPM

SERVICE- LSHF HSD

HEAD- 25 M

PTLFG5

80Oslash

PTLFG6

200X100 PTLFG2

100mmDIA

TO TANK

150m

mDIA

PTLFG8


200mmDIA

80mmDIA

PTLFG12

150m

mDIA

PI PI

200mmDIA

200X150

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TLF PUMP HOUSE

150m

mDIA

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FO

100mmDIA

mas

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MFHSDG1

MP H

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(281)

(282)

(280)

(277)

(278)

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5

300m

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400mmDIA

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P-1

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5M

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0KW

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PM

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FLOW

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HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

200m

mDIA

ST-B

S-1

ST-B

S-2 300Oslash

300mmDIA

PMG8

PMG9

PMG10

PMG11

300X200

300X200

NRV

PMG7

PMG3

PMG4

PMG5

PMG6

NRV

300X200

PMG2

300X200

300mmDIA

TO H

B

TO H

MR

PMG13

PMG 1

4

PMG 1

5

PMG 1

6

PM M

OV 1

M

HSD

HSD

300m

mDIA

SKO

M M MCPMOV30(1

86)

CPMOV29(1

85)

CPMOV28(1

84)

800X300

800X500

800X500

M M MCPMOV31(1

83)

CPMOV32(1

82)

CPMOV33(1

81)

SB

SB

SB

SB

SB

SB

SB

SB

MCPMOV40(1

95)

HSDTO M10M11

HSDTO M8

M

CPMOV38(1

76)

300mmDIA

MMSB

CPMOV51

CPMOV52

80m

mDIA

DRAIN

SB

SB

MCPMOV49

MCPMOV48

MCPMOV46

M

MCPMOV47

MCPMOV43

SB

SB

SB

SB

SB

SB

M CPMOV41

SKO TO M7MCPMOV42

200mmDIA

200mmDIA

PSRN G4

DETAIL

OF P

UMPS( T

RANSFER P

UMP H

OUSE)

P-1

HSD B

URGE L

OADIN

G P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-2

SKO H

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IPE L

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MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0M

MOTOR--6

7KW

1470 R

PM

BOOSTER P

UMP

MAKE--C

GL

MAKE--C

GL

HSD H

B P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-3

P-4

SKO H

MR B

OOSTER P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

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FLOW

RATE--1

60 L

PS

HEAD--5

5 M

MOTOR--1

10KW

1485 R

PM

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-5

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

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MAKE--S

AM

SKO H

MR P

UMP

P-6

FROM R

EFIN

ARY

100mmDIA

300m

mDIA

LOAD A

RAM

LOAD A

RAM

LOAD A

RAM

FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

mDIA

500m

mDIA

300m

mDIA

300mmDIA

300mmDIA

700m

mDIA

700m

mDIA

MM

CPMOV36(1

74)

CPMOV37(1

75)

80m

mDIA

DRAIN

80m

mDIA

DRAIN

80m

mDIA

DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

PTLFG15

PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

PHSG135

PHSG135

FROM T

ANK

200X80400m

mDIA

PHSG120

PHSG116

PHSG117

TO

PMG 1

2

300m

mDIA

300m

mDIA

PMG 1

8PMG17

JETTY-1

PHSG72

200mmDIA

PHSG74

PHSG73

PHSG63

PHSG92

PHSG116

PHSHB114

PHSG109

PHSG117

PHSHB113

PMG 1

2

PHSG63

300m

mDIA

200m

mDIA

700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

mDI A

300mmDIA

300m

mDIA

150m

mDIA

NRV

150m

mDIA

400mmDIA

150m

mDIA

150m

mDIA

80mmDIA

200mmDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50











Flow Rate(klhr)

OriginatingStation

IPS DeliveryStation

TerminalStation



Line Size MAOP




312 Hydraulics

Stage-I


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude(m)

SDH(mcl)

RH(mcl)

No ofMLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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400mmDIA

400mmDIA

400mmDIA

400mmDIA

400mmDIA

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300mmDIA

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100mmDIA

300m

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LOAD A

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FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

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500m

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300m

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300mmDIA

300mmDIA

700m

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700m

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DRAIN

80m

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DRAIN

80m

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DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

PTLFG15

PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

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PHSG135

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PHSG120

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PHSG117

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300m

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300m

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200mmDIA

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PHSG73

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300m

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200m

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700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

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200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

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300mmDIA

300m

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300mmDIA

300m

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150m

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150m

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400mmDIA

150m

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150m

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80mmDIA

200mmDIA

400m

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400m

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400m

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400m

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400m

mDIA

400m

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400m

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Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1




































































33 Pipeline Route















33 Pipeline Route















33 Pipeline Route





















40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION













40 CAPITAL COST


50 OPERATING COST



60 CONDEMNATION


















144 167






















144 167






















144 167
















-- --










-- --










-- --

INTRODUCTION




CHAPTER - I

10 INTRODUCTION




















pipeline
















Terminals






Jharkhand












CHAPTER ndash II









































the pipeline







Fig in MMTPA








2012-13 125 2013-14 101 2014-15 121




Assumptions



Findings










2018-19 2021-22


Haldia- Jasidih 1930 128 43 2100 3424 484 87 3995

Jasidih-Barauni 1567 44 0 1611 3008 382 49 3440


By rail 137 0 27 164 143 0 11 154

Coastal input 808 32 0 840 0 0 0 0








logistics















Rs17 crore




2021-22















































28 Design Capacity













DESIGN PHILOSOPHY




CHAPTER - III


31 Introduction


report






characteristics













crossings

PROJECT DESCRIPTION




CHAPTER - IV


41 Introduction





42 Pipeline Sizing










Flow Rate (klhr)

Originating Station


Terminal Station



Line Size MAOP







Hydraulics

Stage-I


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 1089 - 2+1

2 Barauni 535 46 50

Stage-II


Altitude (m)

SDH (mcl)

RH (mcl)

No of MLPUs

1 Haldia 0 5 757 - 2+1

2 Bolpur (IPS) 206 48 1109 50 2+1

3 Barauni 535 46 50













HBPL Barauni





Haldia











service








requirement













the capital cost

46 Pipeline Route










Annexure-III












47 Civil







as 250m x 130m























491 Mechanical






























VFD








410 Electrical























4103 Bolpur Station















considered
































































Gbps)







RCP Stations 3 Nos

SV locations 37 Nos








location













locations









































































4173 Tankages








419 Condemnation


proposed scheme












Annexure-IV








re-deployed





CHAPTER -V




















Committees

































































regulations
















Petrochemicals
















provided



















pollution







































defined





infrastructure

CAPITAL COST




CHAPTER -VI

60 CAPITAL COST



















Refineries Division










SVs and RCPs only

































614 Escalation





OPERATING COST




CHAPTER - VII

70 OPERATING COST











74 Utilities







75 Manpower



re-deployed









FINANCIAL ANALYSIS




CHAPTER - VIII




















144 167












CONCLUSIONS AND

RECOMMENDATIONS




CHAPTER - IX








reasons









pipeline





































Stage-I







recommendations

--- ---


0 50 100 150 200 250 300 350 400 450 500 550

Chainage (Km)

Hea

d (M

CL)

Station

Chainage (km)

Altitude (M)

Haldia

0

5



211

339

Bolpur (Scraper)

Elevation Profile

1089 mcl

251 mcl

50 mcl

SDH Profile

MAOP Profile

Peak

662 mcl

206

48

535

46


200

385

Jasidih

176 mcl


Haldia PS (Ch 0 km)






SCRAPER BARREL

VALVES

Annexure - II

18rdquo OD



18rdquo OD

18rdquo OD

18rdquo OD


Asansol

Haldia

Barauni

Jasidih



SN MONTHS---gt 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36

ACTIVITY



3






9 Commissioning

LEGEND



An

ne

xu

re-IV


SCADA WORKS


Page 1 of 12

Annexure-V


Capital Cost


(Rs in Lakh)





0 1954 1954







Sub-total 692 87880 88572









Total 727 103030 103757



Annexure-VI




(Rs in Lakh)




3 Manpower 0


a) Mainline 564


5

6


Chemicals

0

40

Total 1883

(Say Rs 19 crore)




Regards








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PI PI

200mmDIA

200X150

PTLFG14

TLF PUMP HOUSE

150m

mDIA

LSHS HSD

FO

100mmDIA

mas

MFHSDG2

MFHSDG1

MP H

SD 9

(281)

(282)

(280)

(277)

(278)

MF H

SD 7

5

300m

mDI A

400mmDIA

P-2

P-1

MS P

UMP H

OUSE

MAKE- K

I RLOSKER

FLOW

- 160S

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

MAKE- K

I RLOSKER

FLOW

- 160LPS

HEAD- 5

5M

MOTOR- 9

0KW

1488 R

PM

200m

mDIA

ST-B

S-1

ST-B

S-2 300Oslash

300mmDIA

PMG8

PMG9

PMG10

PMG11

300X200

300X200

NRV

PMG7

PMG3

PMG4

PMG5

PMG6

NRV

300X200

PMG2

300X200

300mmDIA

TO H

B

TO H

MR

PMG13

PMG 1

4

PMG 1

5

PMG 1

6

PM M

OV 1

M

HSD

HSD

300m

mDIA

SKO

M M MCPMOV30(1

86)

CPMOV29(1

85)

CPMOV28(1

84)

800X300

800X500

800X500

M M MCPMOV31(1

83)

CPMOV32(1

82)

CPMOV33(1

81)

SB

SB

SB

SB

SB

SB

SB

SB

MCPMOV40(1

95)

HSDTO M10M11

HSDTO M8

M

CPMOV38(1

76)

300mmDIA

MMSB

CPMOV51

CPMOV52

80m

mDIA

DRAIN

SB

SB

MCPMOV49

MCPMOV48

MCPMOV46

M

MCPMOV47

MCPMOV43

SB

SB

SB

SB

SB

SB

M CPMOV41

SKO TO M7MCPMOV42

200mmDIA

200mmDIA

PSRN G4

DETAIL

OF P

UMPS( T

RANSFER P

UMP H

OUSE)

P-1

HSD B

URGE L

OADIN

G P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-2

SKO H

B P

IPE L

INE

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0M

MOTOR--6

7KW

1470 R

PM

BOOSTER P

UMP

MAKE--C

GL

MAKE--C

GL

HSD H

B P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--8

33

3 L

PS

HEAD--6

0 M

MOTOR--6

7KW

1470 R

PM

P-3

P-4

SKO H

MR B

OOSTER P

UMP

MAKE--K

IRLOSKER

TYPE-C

ENTRIF

UGAL

FLOW

RATE--1

60 L

PS

HEAD--5

5 M

MOTOR--1

10KW

1485 R

PM

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-5

MOTOR--1

10KW

1450 R

PM

HEAD--5

5 M

FLOW

RATE--1

60 L

PS

TYPE-C

ENTRIF

UGAL

MAKE--S

AM

SKO H

MR P

UMP

P-6

FROM R

EFIN

ARY

100mmDIA

300m

mDIA

LOAD A

RAM

LOAD A

RAM

LOAD A

RAM

FM

FM FM FM

700mm DIA

500mm DIA

300mm DIA

300mm DIA

500m

mDIA

500m

mDIA

300m

mDIA

300mmDIA

300mmDIA

700m

mDIA

700m

mDIA

MM

CPMOV36(1

74)

CPMOV37(1

75)

80m

mDIA

DRAIN

80m

mDIA

DRAIN

80m

mDIA

DRAIN

400mmDIA

400mmDIA

400mmDIA

400mmDIA

TO TANK M-5

TO TANK M-4

TO TANK M-3

TO TANK M-2

100mmDIA

PTLFG15

PTLFG16

PHSG130

400mmDIA

PHSG131

PHSG132

PHSG136

PHSG135

PHSG135

FROM T

ANK

200X80400m

mDIA

PHSG120

PHSG116

PHSG117

TO

PMG 1

2

300m

mDIA

300m

mDIA

PMG 1

8PMG17

JETTY-1

PHSG72

200mmDIA

PHSG74

PHSG73

PHSG63

PHSG92

PHSG116

PHSHB114

PHSG109

PHSG117

PHSHB113

PMG 1

2

PHSG63

300m

mDIA

200m

mDIA

700mmDIA

400mmDIA

300mmDIA

400mmDIA

300m

mDIA

400m

mDIA

200mmDIA

300mmDIA

300mmDIA

100m

mDIA

150m

mDIA

300mmDIA

300mmDIA

300mmDIA

300mmDIA

400mmDIA

400mmDIA

400mmDIA

400m

mDIA

300mmDIA

300m

mDI A

300mmDIA

300m

mDIA

150m

mDIA

NRV

150m

mDIA

400mmDIA

150m

mDIA

150m

mDIA

80mmDIA

200mmDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

400m

mDIA

Slide Number 1

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-FINALpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

Separatorspdf

EXECUTIVE SUMMARY

INTRODUCTION


DESIGN PHILOSOPHY

PROJECT DESCRIPTION


CAPITAL COST

OPERATING COST

FINANCIAL ANALYSIS

CONCLUSIONS

AND

RECOMMENDATIONS

ANNEXURE amp

APPENDICES

DFR-CONTENTpdf

31 Introduction





CHAPTER - IV

41 Introduction

42 Pipeline Sizing


Hydraulics

Stage-I

Stage-II






46 Pipeline Route





47 Civil



491 Mechanical

410 Electrical











4103 Bolpur Station






























RCP Stations 3 Nos

SV locations 37 Nos























4173 Tankages




419 Condemnation






CHAPTER -V

CHAPTER -VI

CHAPTER - VII

CHAPTER - VIII

CHAPTER - IX

5HY-GRAD-SCHEMEpdf

Slide Number 1

Slide Number 2

ROUTE MAPpdf

Slide Number 1

ROUTE MAPpdf

Slide Number 1

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