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LENNIIHIMMASH GROUP
St. Petersburg
LENNIIHIMMASH Group owns a 10-storey building on
Vasilyevsky Island of St. Petersburg.
2
Business-model of LENNIIHIMMASH GROUP
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Complex Engineering
Research and Development
• Intellectual property
• Now-how in engineering processes optimization
• Feasibility analyses works (feasibility calculation,
feasibility study, feasibility analyses of investments)
• Scientific research developments
• Engineering consulting
• Basic designs (FEED)
• Design and detailed design documentation in
conformity with the law of the Russian Federation
• Getting approval of state expert review bodies
ЕРС-, ЕРСm-
strategies • Management of projects
• Equipment supply
• Construction and installation works
• Supervised installation and commissioning
• Engineering support of the Customer (consulting)
LNHM fulfills a complete cycle of works from concept development of a
production facility to its start up
LENNIIHIMMASH GROUP field of expertise
Gas processing,
gas liquefaction Gas-to-chemicals
Chemical and
metallurgical facilities
Treatment (complex purification, dehydration,
desulfurization) and liquefaction of natural gas
Low-temperature gas processing with recovery of
Dry Gas and C3 +
Stabilization of gas condensate and gas
fractionation
Deep gas processing with recovery of ethane fraction
and helium concentrate
Storage and transportation of gas and gas products
Production (pyrolysis): ethylene, propylene
Rectifying separation and purification of olefins
High-pressure polymerization of ethylene
Methanol production
Equipment design for organic synthesis processes (LD and HD polyethylene,
bisphenol - A, polycarbonate, etc.)
Trichlorosilylane and tetrachloride synthesis in
EB reactor
Condensation of steam-gas mixtures of
Trichlorosilylane synthesis and silicon hydrogen recovery
Rectifyng separation and purification of
trichlorosilylane, tetrachloride, hydrogen
chloride, etc.
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Off-site facilities and utilities (water supply and sewerage, office building, power supply, fire station, central control room etc.)
Advantages of LENNIIHIMMASH GROUP
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Research and Development
Now-how in engineering: proprietary data base with technical/design solutions based on accumulated experience
Proprietary (incl. patented) practices in process solutions and main equipment
Digital 3D-model of production facility
Pre-design technical and process consulting
Insuring required process parameters (recovery rate of target components, quality and quantity of products etc.) of facilities operations
Decreasing terms and costs of engineering works
Systematization of accumulated long-term experience
Orenburggazprom LLC
UDP Shurtanneftegas
OAO Surgutneftegas
Severorgsintez ZAO
OAO Usolye Siberian Silicone
OAO Gubkinsky GPC
OAO Noyabrsky GPC Vyngapurovsky GPP
OAO Yuzno-Baluksky GPC
OAO LULOIL-PNGP Geography of major projects
executed over the last 10 years ZAO Sibur HIMPROM
PAO Kazanorgsintez
KINEF, LLC
LUCOIL
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ОАО SiburTyumenGaz Vyngapurovsky GPP expansion.
Construction of GPU No. 2.
Advantages of LENNIIHIMMASH GROUP
Advantages of LENNIIHIMMASH GROUP Figures of the major projects
Over the last 10 years LENNIIHIMMASH GROUP has designed/built gas processing facilities with
total capacity of 12.5 bln m3 APG/year
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Indicators Units
ZAO
Severorgsintez
2006-2008
OAO Gubkinsky
GPP
2009-2010
OAO Noyabrsky
GPC
Vyngapurovsky
GPP
2010 -2012
OAO Yuzhno-
Balyksky GPP
2010-2012
LUKOIL –
Permneftegas
pererabotka,
LLC
2012-2014
OAO Siburtyumen-Gaz
Expansion of
Vyngapurovsky GPP.
Construction of GPU No.
2
2013-2015
PAO Kazanorgsintez
Revamp of Ethylene
plant
2017-2019
CAPEX for the project mln
USD 108,0 67,0 172,0 79,0 234,0 275,0 92,0
Investment utilization
share of LNHM group
mln
USD 56,0 33,5 94,0 57,0 166,0 202,5 17,3
Total period of project
execution month 24 19 24 24 26 24 23
Period of project
execution by LNHM
group
month 18 14 22 20 20 22 19
Deviation from the
customer’s budget
accepted by the
investment committee
As a rule 2.5-3 years
prior to commissioning
% +10% -3% +3% +7%
At detailed
design
documentation
stage under the
contract
Fix EP – +
1.5%
At detailed design
documentation stage
+2.6% +1,5%
Volume of works completed by LENNIIHIMMASH GROUP
8
0
5
10
15
20
25
2012-2018
Billion Rubles
Total works Procurement Engineering
LNHM Group turnover in 2012-2018 was 23,11 bln. Rubles
Structure of the turnover is indicated in the diagram
Total number of LENNIIHIMMASH GROUP employees is 310 people. Headcount of engineering-technical staff is 260 persons,
Including 12 Ph.Ds in technical sciences.
Advantages of LENNIIHIMMASH GROUP
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Complex engineering
Experience of joint projects with leading foreign licensors of specific technological processes
Collaborative initial data collection and complex engineering (preFEED, FEED, design an detailed design documentation)
Equipment selection in line with maximal import substitution. Adapting of licensor’s documentation to the codes and regulations of
the Russian Federation
Forming and supporting the necessary documentation; passing and getting approval of Glavgosexpertiza (State expert review) for design
documentation, State Ecological review, Industrial safety expert review
Author’s supervision of construction
Decreasing Capex level and cost of design and survey works by minimum 25% due to import substitution and optimizing appliance of design codes and
regulations of the Russian Federation
Accelerating implementation of revamp projects of operating facilities by minimum a year
Cooperation with foreign licensors
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Interaction in projects with joint participation of foreign and
Russian EP-contractor
1) Contract strategy convenient for the Customer is based on the Technical assignment combined for the Russian and foreign contractors with a detailed responsibility assignment matrix of the parties
2) Arrangement of shared access to information (for example, ftp-service with shared access)
3) Integrated engineering schedule
(combined work schedule of Customer, foreign contractor and
Russian contractor)
4) Integrated reporting of foreign and Russian contractors
5) Weekly skype conference calls
Detailed description of cooperation experience with Technip is shown in the Attachment
Successful practice of arranging interaction between
Customer, foreign EP-contractor and Russian EP-contractor
Advantages of LENNIIHIMMASH GROUP
Advantages of LENNIIHIMMASH GROUP
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ЕРС contract strategy
Engineering (process/technical) consulting
Initial data collection and feasibility analyses works
Complex engineering (basic project (FEED), design and detailed design documentation
Getting approvals of state expert review bodies
Preparation of ITB tender package (if necessary)
Complex purchasing of equipment and its delivery to site
Construction and installation works
Commissioning works, ramping-up to the rated parameters and facility start-up
Decreasing Capex for project implementation
Substantial acceleration of production facilities start-up
Implementation of “turn-key” projects (ЕРС)
Mitigation of risks (possibility) of start-up failure of the facility
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Advantages of LENNIIHIMMASH Group
Implementation of “turn-key” projects (ЕРС) Main stages
Engineering consulting
Feasibility analyses Complex engineering
Поставка оборудования
Construction and installation works.
Facility commissioning and start-up
Interacting with Customers on feasibility stages: giving consultations on process technology, equipment, operation conditions Analyses of markets Ensuring cooperation with Licensors Feasibility analyses works (feasibility calculation, feasibility study, feasibility analyses of investments, main technical solutions)
Choice and substantiation of the Licensor (if necessary) Basic engineering(FEED, preFEED) Design and detailed design stages Passing the necessary expertise reviews and getting the approval of State ecological expertise and Glavgosexpertiza for design documentation Preparation if necessary of tender documentation package (ITB)
Tender procedures, selection of contractors, purchasing equipment Development of the most efficient logistics schemes for transportation Equipment delivery to site
Construction and installation works Supervised installation Pre-commissioning works Commissioning and start-up Engineering consulting: technical support in the process of operation
Advantages of LENNIIHIMMASH GROUP
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Traditional project implementation schedule – from 49 months
Standard project implementation schedule in LENNIIHIMMASH GROUP– from 25 to 27 months
Design Stage (Stage “Project”)
State Expertise and Ecological Expertise
Detailed Design Stage
Procurement
Civil and Installation Works
Commissioning and start-up
Design Stage (Stage “Project”)
State Expertise and Ecological Expertise
Detailed Design Stage
Procurement
Civil and Installation Works
Commissioning and start-up
3 mos.
27 mos.
49 mos.
6 mos.
6 mos.
6 mos.
6 mos.
12 mos.
12 mos.
20 mos.
20 mos.
18 mos.
16 mos. 3 mos.
Project implementation time saving – around 40% or 20-22 mos.
Implementation of “turn-key” projects (ЕРС)
Comparison of implementation schedules
The advantage of the ЕРС-strategy is based on possible simultaneous execution of stages of design works and process equipment purchasing
Complex Engineering
Design Engineering
Total number of the engineering department personnel is 188 employees.
Total man / hours per year – 340 000
• Inspections and engineering surveys • Pre-design works (feasibility study etc.) • Basic engineering (Stage "Project") • Detailed design (Stage"detailed design
documentation”) • Support of the design documentation during
state expertise (Glavgosexpertiza) • Author Supervision of construction • Pre-commissioning • Expert assessment of the design and
detailed design documentation
Main types of engineering works:
Technical personnel of the engineering department
Position numb.
Executives, chief project engineers 11
Process engineers 30
Installers, application engineers 42
Automation and control specialists 11
Electric engineering specialists 12
Construction experts (total): 64
- steel structure designers 21
- concrete structure designers 18
- architects 6
- plot plan experts 4
- water supply and sewerage, heating and ventilation experts
15
Estimators 9
CAD experts 9
15
Technological process modelling Design Engineering
AspenONE for Process Engineering
Product Purpose
Aspen Air Cooled Exchanger
Design and calculation of air refrigerators
Aspen HYSYS® Modelling, design of chemical and technological plants, control of equipment productivity
Aspen HYSYS® Amines
Calculation of purification of gas and liquid hydrocarbon media from CO2 and H2S with alkanolamine solutions
Aspen HYSYS® Crude
Allows to set oil sample values in the programme and to model VDU columns.
Aspen MUSE Design and calculation of plate heat exchangers used in gas-separation process
Aspen Plate Exchanger
Design and calculation of plate heat exchangers for the chemical and oil industries
Aspen Plate Fin Exchanger
Design and calculation of plate heat exchangers
Aspen Process Economic Analyzer
Forecasts cash flows and operational costs in design
Aspen Shell & Tube Mechanical
Design and mechanical calculation of shell-and-tube heat exchangers, and pressure vessels
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LENNIIHIMMASH GROUP, LLC has a single integrated design environment, including 3D
modeling and 2D process solutions
AVEVA Diagrams
AVEVA
Instrumentation
AVEVA PDMS
(3D model)
Issuance of all types of
detailed design
documentation
Process flow diagram
Installation connection diagram
Lists of valves, equipment, lines
Data sheets for valves
Pipe grades
Equipment layout
Pipe routing, installation of valves and
instruments
Development of steel and r/c
structures
Development of buildings and
structures
Cable routing
Heating and ventilation system
installation
Development of water supply and
discharge systems
Data sheets for instruments
Electric schematic control and monitoring
diagrams
Connection diagrams for the external wiring of
the junction boxes
Cable list
Instrument installation diagrams
Number of AVEVA licenses– 65
Documentation development based on 3D model
Design Engineering
Outgoing documentation is generated based on the developed model (plans, views, sections, material requisitions, isometric drawings)
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Installation of equipment, piping systems and steelwork in 3D model
Design Engineering
Solid Works
Software system for 3-dimensional design of equipment, piping assemblies and documentation development in accordance with the Unified System for Design
Documentation.
Number of Solid Works licenses – 20.
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Process modeling (HYSYS)
• Optimum choice of heat-insulating designs and materials • Calculation of the required minimum heat-insulation layer thickness • Selection of standard sizes of products • Calculation of work scopes and total quantity of materials • Issue of design
documentation
Design Engineering
Insulation
ANSYS Structural
Strength calculation by method of finite element analysis Calculation of static, cyclic, seismic and vibration strength of pipeline systems of petrochemical and oil processing facilities
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Project Management
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III quarter
(August-
September)
IV quarter I quarter II quarterIII quarter
(July)
340 918 59 288 89 448 79 630 80 840 31 712
214 062 47 993 87 093 54 162 19 905 4 909
126 856 11 294 2 354 25 467 60 935 26 803
ParameterTotal as of
2019-2020
LENNIIHIMMASH Group (total)
2019 2020
Maximum availability, man/hour
Availability reserve, man/hour
Current project portfolio, man/hour
Projects with long execution period are managed and monitored using the method
of calendar and network planning via PRIMAVERA software
Data on workload of design division departments of LENNIIHIMMASH Group
Workload reserve Workload of design division departments
Workload reserve of design division departments for the period
August 2019 – July 2020, man-hour
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III quarter
(August-
September)
IV quarter I quarter II quarterIII quarter
(July)
7 245 622 126 1 421 3 520 1 556
20 512 1 522 392 4 767 9 663 4 168
30 763 2 904 638 6 386 14 630 6 205
6 828 523 94 904 3 726 1 580
5 846 395 42 326 3 413 1 668
13 216 1 269 246 2 901 6 180 2 620
15 115 1 416 304 3 220 7 146 3 030
3 994 270 62 836 1 986 841
2 717 205 46 635 1 287 545
3 690 337 58 873 1 702 721
3 751 489 47 264 1 685 1 266
7 532 721 168 1 781 3 414 1 448
Construction design division. Plot plan sector
Water supply and sewarage sector
Construction design division. Heating and
ventilation sector
Estimating department
Construction design division. Architectural
sector
Assembly division. Configuration, pipelines
and pipe racks sectors
Automation and communication division
Electrical engineering division
Construction design division. Group of
reinforced concrete structures
Construction design division. Group of steel
structures
Management personnel (executive heads,
chief and deputy chief project engineers)
Process division
DivisionTotal as of
2019-2020
Availability reserve of Design Engineering divisions, man/hour
2019 2020
Engineering department
Labour force
23
Number of divisions of Engineering Department, man/hour in total: 188
Management (executive heads, chief project engineers, deputy chief project engineers)
11
Process division 30
Assembly division. Configuration, pipelines and pipe rack sectors 42
Automation and communication division 11
Electrical engineering division 12
Construction design division. Group of reinforced concrete structures. 18
Construction design division. Group of steel structures. 21
Construction design division. Architectural sector 6
Construction design division. Plot plan sector 4
Water supply and sewerage sector 10
Construction design division. Heating and ventilation sector 5
Еstimating department 9
CAD group 9
Main technical and economical indicators of the unit:
for APG- 900 mln.st.m3/year; for additional wide fraction of light hydrocarbons
(WFLH) - 512 thousand tons/year.
Content of target components: C3+ - 224 g/st. m3 (WFLH); C2+ - 367g/st. m3 (eWFLH).
Content of target components in Dry Gas: not more than 5 g/st.m3 when receiving WFLH.
Product output volume: • Dry stripped gas (1.8 MPа, 41°С) – 737.3 mln. st.
m3/year • Ethane fraction(2.1 МPа, 42°С) – 75.6 thousand
tons/year • Propane fraction (1.37 МPа, 43°С) – 296.5
thousand tons/year • Propane-butane-pentane fraction (0.8 МPа, 43°С) –
119.7 thousand tons/year • Iso-butane fraction (1.01 MPa, 43°С) – 80.7
thousand tons/year • N-butane fraction(1.0 МPа, 40°С) – 192.7 thousand
tons/year
Recovery factor C3+ 98%
“LUKOIL – Permneftegaspererabotka” OAO
Start of project– July 2012, Completion of project– December 2014
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Reconstruction of “NTKR” (low temperature condensation and rectification) unit. Construction of the
second stage of APG processing plant
CAPEX for the project: 234 mln. $ Investment utilization share of LENNIIHIMMASH Group: 166 mln. $
Functions of LENNIIHIMMASH Group:
• General designer (development of process, design and detailed design documentation. Obtaining approval of Glavgosexpertiza of Russia.
• Supplier of process equipment. • Author supervision of construction, installation of
equipment and commissioning works.
“LUKOIL - Permneftegaspererabotka” OAO
25
Main figures of the project
More than 3000 tons Volume of the supplied equipment
5 820 20 720 pcs.
Control System signals - physical - digitally transmitted from local automated systems
Operator’s human-machine interfaces
(HMI), servers, printers, optic-fiber
connection etc. (based on Yokogawa equipment)
DCS of technological process
DP-6kV pcs. Electrical equipment
55 (Air-cooling devices – 5 pcs.) pcs. Rotating equipment.
123 pcs. Static equipment
Permneftegas-pererabotka Unit Item
26
“LUKOIL – Permneftegaspererabotka” OAO
Petroleum gas compressor station
stenching block
Outdoor dryer and gas fractionation unit
Outdoor low-temperature condensation and rectification unit
Main technical-and-economic indicators of the unit:
1.4 billion m3/year on hydrocarbon gas
Content of target components in APG: С3+ - 301.1 g/nm3.
Content of target components in Dry Gas: not more than 3 g/nm3.
Product output volume:
• Dry gas (7.5 МPа, 40 °С) 0.951 billion st.m³/year;
• WFLH (3.7 МPа, 40 °С) 398.2 thousand tons/year.
Recovery factor C3+ 99,4%
Start of project– September 2013
Completion of project– November 2015
27
Construction of new facility for APG processing
CAPEX for the project: 275 mln. $
Investment utilization share of
LENNIIHIMMASH Group : 202.5 mln. $
Functions of LENNIIHIMMASH Group:
• General designer (development of process, design and detailed design documentation). Obtaining approval of Glavgosexpertiza of Russia.
• Supplier of equipment and materials above and below ground level.
• Supervision of construction and installation of equipment.
• Commissioning works.
“SiburTyumenGaz” OAO Expansion of Vyngapurovsky GPP
More than 2 300 tons Volume of the supplied
equipment
1 906 tons
Piping(no fittings)
3 525 tons Steel structures
6 653 м3 Concrete
3 350 pcs. Piles (reinforced)
Materials for installation and construction works
2 557 7 990
(from compressors– 1558, Turbo expanders - 200)
pcs. Control System signals
- physical - digitally transmitted from local automated systems
Operator’s HMI, servers, printers, optic-fiber
connection etc. (based on Метsо equipment, Finland)
DCS of technological process
PTS-1, PTS-6 – 2
pcs.
Electrical equipment
52 (Air cooling devices – 26 pcs.)
pcs. Rotating equipment
41 pcs. Static equipment
Vyngapurovsky GPP-2 Unit Item
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“SiburTyumenGaz” OAO Expansion of Vyngapurovsky GPP
Main figures of the project
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“SiburTyumenGaz” OAO Expansion of Vyngapurovsky GPP
No on PP Name of Unit
210 Preliminary Separation unit
211 Compressor station №1
212 Dehydration unit
213 Furnace unit
214 Low-temperature Condensation and Rectification unit
215 Turbo-expanding unit
216 Compressor station №2
217 Methanol Injection unit
218 Fuel Gas Treatment unit
219 Heat Transmission unit
Explication of the main processing facilities of VGPP-2
VGPP-1
VGPP-2
“Noyabrsk GPC” OAO Vyngapurovsk GPP
Start of Project– August 2010,
Completion of Project – September 2012
30
CAPEX for the project : 172 mln. $
Investment utilization share of
LENNIIHIMMASH Group : 94 mln. $
Construction of GPP with recovery of ethanized WFLH
Main technical-and-economic indicators of the unit : 2.1 billion m3/year of hydrocarbon gas Content of target components :
C3+ - 209 g/m3 (WFLH)
C2+ - 348 g/m3 (ethanized WFLH)
Content of target (C3+) components in DSG: 5 g/m3 at receiving WFLH
3 g/m3 at receiving eWFLH
Total product output: • Dry gas (6.0 MPа, 45 °С) 1.581-1.758 billion
m³/year • WFLH (3.5 MPа, 20-40 °С) 349.2 th. t/year • eWFLH (3.5 МPа, 20-40 °С) 561.6 th. t/year
Extraction factor C3+ 99%
Functions of LENNIIHIMMASH Group:
• General designer (development of process, design and detailed design documentation). Obtaining approval of Glavgosexpertiza of Russia.
• Supplier of equipment and materials above ground level.
• Supervision of construction and installation of equipment.
• Commissioning works.
Over 2 000 tons Volume of supplied
equipment
1 258 tons
Piping (without fittings.)
1 468.45 tons Steel structures
6 318 m3 Concrete
2 890 pcs. Piles (reinforced)
Materials for construction and installation works
1 850 2 000
(from compressors– 1 800, turboexpanders - 200)
pcs.
Control System signals: - physical;
- digitally transmitted from local automated systems
Operator’s HMI, servers, printers, optic-fiber connection etc (based
on Metso equipment, Finland)
DCS of technological process
Transformer substations – 3 Outdoor switchgear– 1
Emergency shutdown system panel- 1
pcs.
Electrical equipment
21 (Air-cooling devices – 13 pcs.) pcs.
Rotating equipment
30 pcs. Static equipment
Vyngapurovsk GPP-1 Unit Item
31
Main figures of the project
“Noyabrsk GPC” OAO Vyngapurovsk GPP
32
No on PP Name of unit
700.1 External gas fractionation unit
700.2 Turbo expanding unit
700.4 DSG compression unit
701 Gas dehydration unit
402.1 Panels
402.2 PCS-3
Explication of construction facilities
“Noyabrsk GPC” OAO Vyngapurovsk GPP
PAO “Kazanorgsintez” Ethylene Plant
33
Start of project– November, 2017
Actual completion of Stage 1 – September, 2018 года
End of project planned – September, 2019
CAPEX for the project– 92 mln. $
Investment utilization share of LENNIIHIMMASH Group as of November, 2018 – 17,3 mln. $
Main technical-and-economic indicators :
Feedstock:
before reconstruction
• Ethane – 62% • Propane – 10% • Other fractions– 28% after reconstruction
• Ethane – 52% • Propane – 30% • Other fractions– 17%
Market product:
before reconstruction– 100%
• Ethylene – 93%
• Propylene – 7%
after reconstruction– 118,3%
• Ethylene – 86%
• Propylene – 14%
Reconstruction of plant workshops: Revamp and retrofit of functioning production
facilities
34
Functions of LENNIIHIMMASH Group :
• Development of design and detailed design documentation, as well as documentation
for retrofit according to the basis of design of “Technip” company.
• Obtaining approval of Glavgosexpertiza of Russia (stage P) and industrial safety expert
review (documentation for retrofit)
• Supply of main process and auxiliary equipment
PAO “Kazanorgsintez” Ethylene Plant
As a result of the reconstruction the following goals will be achieved:
• Increase of product output volume
• Diversification of feedstock (increase of propane share in processing)
• Increase of consistency and safety of production facilities due to replacement of outmoded
and worn out equipment of E-100, E-200 and E-500 plants
• Increase of production efficiency and decrease of production expenses
• Decrease of prime cost of output product
(see attach.)
35
Four cell cracking furnace – 1 pcs.
(operation possible on ethane as well as propane feed)
Column equipment – 3 pcs.
(propane-propylene fraction splitter 2pcs. ,
condensate stripper 1pcs.)
Electric motors – 3 pcs.
(2pcs. 10 МW 1 pcs. 13,5 МW)
Cold box– 1 pcs.
Pumps – 30 pcs.
(Centrifugal– hermetic al 16 pcs., Centrifugal 14 pcs.)
Pressure reducing cooling units – 4 pcs.
(packaged design)
Heat exchangers – 43 pcs.
(1- plate heat exchanger
42 shell and tube heat exchangers)
Air coolers – 12 pcs.
(zigzag 6 –pcs. horizontal – 6 pcs. )
Vessel equipment– 18 pcs.
(2 packaged design)
Chemical dozing units – 7pcs.
(packaged design)
PAO “Kazanorgsintez” Ethylene Plant Main process units, blocks and
equipment as part of Ethylene plant revamp project
“NK ROSNEFT” OAO “Otradnensky GPP” ZAO
Development of detailed design documentation for Deethanization and Low-temperature Condensation unit
36
Development of the detailed design documentation for 12 modules using CAD SolidWorks for further order placement at the manufacturer. The modular blocks are developed as structurally finished assembly unit with target level of prefabrication in transport dimensions.
Start of project– May 2014
Completion of project– February 2015
240 mln. m3/year on associated petroleum gas;
Content of target components:
C2+ - 700 g/st.m3 (feed gas)
Content of target components in DSG:
C2+ - 228 g/st.m3
Total product output: • DSG - 0.156 billion st.m³/year • Ethane fraction blend «B» - 53.8 mln. tons/year • WFLH – 186.27 mln. tons/year
Recovery factor С3+ no less than 95 %
Main technical-and-economic indicators of the unit :
Functions of LENNIIHIMMASH Group: • Development of detailed design documentation for
the deethanization and low-temperature condensation modular unit.
Recovery factor С2+ no less than 70 %
“Uzhno-Balyksky GPC” OAO
37
Beginning of Project– September 2010 Completion of Project– December 2012
CAPEX for the project : 79 mln. $
Investment utilization share of
LENNIIHIMMASH Group : 57 mln. $
Main technical-and-economic indicators of the unit : 2 billion m3/year of hydrocarbon gas Content of target components : C3+ 71.35г/m3 (WFLH) C2+ 174.7/m3 (eWFLH)
Content of target (C3+) components in DSG:
5 g/m3 at receiving WFLH
3 g/m3 at receiving eWFLH
Total output:
• Dry gas (1.19-132 MPа, 14.5-35°С) 1.81-1.92 billion m³/year
• WFLH (3.65 MPа, 9-40 °С) 140.4 th.t/year
• eWFLH (3.65 MPа, 9-40 °С) 293 th.t/year
Extraction factor C3+ 99%
Functions of LENNIIHIMMASH Group: • General designer (development of process, design
and detailed design documentation). Obtaining approval of Glavgosexpertiza of Russia.
• Supplier of equipment and materials above ground level.
• Supervision of construction and installation of equipment.
• Commissioning works.
Construction of new gas processing facility with recovery of ethanized WFLH
“Uzhno-Balyksky GPC” OAO
over 1 500 tons Volume of supplied
materials and equipment
580 tons Piping (without fittings.)
651.1 tons Steel structures
1 293 m3 Concrete
1 260 pcs. Piles (reinforced)
Materials for construction
and installation works
1 020 700
(from compressors– 500,
from turboexpanders – 200)
pcs.
Control System signals: - physical;
- digitally transmitted from local automated systems
Operator’s HMI, servers, printers, optic-
fiber connection etc. (based on Yokogawa
and Меtsо equipment)
DSC of technological process
Transformer substation-1 Emergency shutdown
system panel- 1 pcs. Electrical equipment
26 (Air-cooling devices– 18 pcs.) pcs. Rotating equipment
22 pcs. Static equipment
Uzhno-Balyksky GPC Unit Item
38
Main figures of the project
“Uzhno-Balyksky GPC” OAO
39
No on PP Name of Unit
300.1 Dehydration unit
300.3 External Gas Separation Unit
300.4 Turbo-expanding Unit
301 Transformer Substation КТП-16
302 Methanol Injection unit
Explication of facilities
Main technical-and-economic indicators:
• CSU for non-stabilized gas condensate – 5,44 mln. tons/year
Product output volume: • Deethanization gas– 628 mln. st.m³/year • Technical propane-butane– 667 th. tons/year • Stabilized gas condensate– 4 250 th. tons/year Recovery factorC3+ 99%
• GCS – total flow rate of gas 14.28 bln. st.m³/year
• DCS – total flow rate of gas 833 mln. st.m³/year
40
“ROSPAN INTERNATIONAL” ZAO “TNK-ВР Holding” OAO
Construction project development Condensate Stabilization Unit
(CSU), Gas Cooling Station (GCS) Deethanization Compressor Station (DCS) at
East Urengoy licensed site
Functions of LENNIIHIMMASH Group:
• Development of the design documentation
• Obtaining approval of Glavgosexpertiza of Russia.
Start of project– August 2011 Completion of project– December 2012
tank farm GCS
tank farm LPG
Condensate
stabilization unit
Deethanization
compressor station
Layout of the designed facilities
• The project includes construction of 4 process lines of CSU and one line of unstabilized condensate degassing in traps
• CSU consists of 3 main units – separation unit, deethanization unit, stabilization unit and auxiliary equipment
• The designed facilities also include storages for technical propane-butane and stabilized gas condensate
41
Plot plan solutions for Condensate Stabilization Unit
CTS, panels SGS panel
Fire tank
Furnaces unit Heat carrier
pump station Receivers unit
Heat carrier
intermediate
storage
Control room
CSU
External units
“ROSPAN INTERNATIONAL” ZAO “TNK-ВР Holding” OAO
“Gubkinsky GPC” OAO
42
Start of Project– January 2009
Completion of Project – October 2010
CAPEX for the project : 67 mln. $
Investment utilization share of
LENNIIHIMMASH Group : 33.5 mln. $
Functions of LENNIIHIMMASH Group: • General Designer (development of process, design and detailed design documentation). Obtaining approval of Glavgosexpertiza of Russia • Process equipment supplier • Supervision of construction • Supervision of process equipment installation
Construction of new gas processing facility
with recovery of WFLH
Main technical-and-economic indicators of the unit :
2 billion m3/year of hydrocarbon gas Content of target components (с3+) in APG - С3+ - 100 g/nm3
Content of target components in DSG : no more than 2 g/m3
Total product output:
• Dry gas (1.37 MPа, 45 °С) 1.92 billion st. m³/year
• WFLH (5.5 МPа, 20-40 °С) 146.18 th.t/year
Extraction factor C3+ 99%
“Gubkinsky GPC” OAO
1 038 tons Volume of supplied equipment
233 tons Pipes
431 tons Steel structures
485 m3 Concrete
840
pcs.
Piles (reinforced)
Materials for construction and installation works
1 350 1 200
(from compressor– 1 000, from turboexpander - 200)
pcs.
Control System signals: - physical;
- digitally transmitted from local automated
systems
Operator’s HMI, servers, printers, optic-fiber connection etc. (based
on Metso equipment, Finland)
DCS of technological process
Transformer substation - 1 pcs.
Electrical equipment
10 (Air-cooling devices – 3 pcs.) pcs.
Rotating equipment
7 pcs. Static equipment
Gubkinsky GPC Unit Item
43
Main figures of the project
“Gubkinsky GPC” OAO
44
No on PP
Name of Unit
301 Gas treatment unit
302 Compressor-turbine unit
303 External gas separation unit
303.1 Vent stack
304 Turbo-expanding unit
305 Furnace unit
Explication of facilities
Improvement of layout and process solutions allows for more compact
layout of the designed facilities, which is very important for their
arrangement on site where functioning production plants are
located.
Main technical-and-economic indicators of the facility : 1.5 billion m3/year of hydrocarbon gas
Content of target components: C3+ up to 100 g/st.m3.
Content of target components in DSG: not more than g/st.m3.
Product output volume:
• Dry stripped gas– 1.2 bln. st.m3/year complies with OST 51.40-93; • Auto propane-butane – 96.44 th. tons/year
complies with GOST Р 52087-2003.
“Severorgsintez” ZAO
45
Recovery factor C3+ 94,6%
Construction of Gas Processing Industrial Complex UPBS-100 for
Eastern Urengoy and Northern Esetinsk oil-gas condensate fields
Start of project– April, 2006
Completion of project– July 2008
CAPEX for the project, including tank park: 108 mln. $
Investment utilization share of
LENNIIHIMMASH Group : 56 mln. $
Functions of LENNIIHIMMASH Group: • General Designer (development of process, design and detailed design documentation). • Process equipment supplier • Supervision of construction • Supervision of process equipment installation and commissioning works
“Severorgsintez” ZAO
46
Construction of gas and unstabilized condensate processing facility
1 006 pcs.. Valves
628 pcs. Control system signals
Operator’s HMI, servers, printers,
optic-fiber connection etc..
DCS of technological process
Diesel power station AKSA pcs.. Electrical equipment
33 (Air cooling devices – 8 pcs..) pcs.. Rotating equipment
45 pcs. Static equipment
UPBS-100 Unit Item
“Severorgsintez” ZAO
47
Main technical-and-economic indicators : Volume of liquefied hydrocarbon gases incoming to the park is: Option 1 : auto propane-butane mixture(APB)
according to GOST Р 52087-2003 – 536 m3/day Option 2: propane fraction blend «А» according to
TU 0272-023-00151638-99 – 328 m3/day
Technical butane according to GOST Р 52087-2003 – 208 m3/day
Construction of commodity park
Functions of LENNIIHIMMASH Group: • General Designer (development of design and detailed design documentation, detailed design of process equipment). • Process equipment supplier • Author Supervision of construction • Supervision of process equipment installation and commissioning works
Reception and storage of the liquefied hydrocarbon gases and supply to LPG loading station for filling tank cars or container
tanks
Start of project– April, 2006
Completion of project– July , 2008
“Severorgsintez” ZAO
48
Supplied equipment:
Spherical tanks, 600 m³ each - 8 pcs., including 2 reserve Pumping equipment– 4 pcs. Vessel equipment – 3 pcs. Filters – 4 pcs. LPG loading station Vent stack– 1 pcs.
Construction of commodity park
The scope of supply also included cut-off and safety valves, instrumentation, monitors of product quality control in the pipelines, tanks, at the loading stations and drain vessel.
Time for filling up the commodity park reservoirs is 5.5 days, which complies with item 4.2 IS 09-566-03.
The loading station includes a loading rack with 6 loading points for filling tank cars or container tanks. Odorization of products is provided when necessary.
The commodity park area as per the plan makes 350 х
200 m, which equals 7.0 ha.
The works under this project were completed according to EPC procedures. Engineering, design, release for construction, supply and installation works were performed simultaneously, thus allowing for completion within the shortest time limits.
Raw gas from Kovykta gas condensate field was supposed to be used as a feed.
“Sayanskkhimplast” OAO “Krioplast” ZAO
49
Components Structure, %
mol.
He 0.20
H2 0.05
N2 1.72
CH4 97.87
C2H6 0.23
CO2 0.01
Helium plant as part of Sayansky Complex of natural gas processing and ethylene and helium
recovery
Start of project– May, 2006
Completion of project– July , 2007
Functions of LENNIIHIMMASH Group:
• Development of the design documentation
• Obtaining expert approvals
The capacity of the helium production facility for methane fraction is 4.0 bln. n.m3/year. Fluctuations of productivity from -30% to + 15%.
Product output volume: • Gaseous helium, blend according to TU 0271-135-
31323949-2005 - 546 960 nm3/year • Liquid helium according to US specification «Compressed
Gas Association Inc.» GGA G – 9.1 – 1992, grade N – 10 568 thousand liters.
Helium recovery factor no less than 99 %
Main technical-and-economic indicators of the facility:
Raw gas parameters:
Р – 2.6 MPа (abs.); T – 173 0К
Composition of raw gas: Composition of the recovered helium concentrate:
Composit
ion, %
mol.
Helium
concentrate
composition
Не 71.6
N2 14.9
СН4 traces
Н2 13.5
“Sayanskkhimplast” OAO “Krioplast” ZAO
50
1 – Helium concentrate recovery unit 2 – Liquid nitrogen storage 3 – Compressor 4 – Helium treatment and liquefaction unit 5 – Nitrogen and helium receivers
6 – Helium shipping station 7 – Vehicle inspection point 8 – Cylinder filling unit 9 –Liquid nitrogen car tank loading station 10– Liquid nitrogen railway tank loading station
“Surgutneftegas” OAO
Recovery factor С3+ 98 %
51
Start of project– November, 2003
Completion of project– July, 2006
Functions of LENNIIHIMMASH Group : • General Designer (development of the design and detailed design documentation and process procedures) • Obtaining expert approvals • Supervision of construction
Construction of new gas processing facility with turbo expander of Surgut GPP
Main technical-and-economic indicators
of the unit:
3 bln. m3/year of associated petroleum gas;
Content of target components in APG : С3+ - up to 93 g/nm3.
Content of target components in DSG :
no more than 4 g/ st.m3
Volume of product output:
• Dry stripped gas (GOST 5542-87) – 2.83 bln.st.m³/year
• Propane-butane technical mixture (GOST 20448-90) – 132.7 thousand tons/year
• WFLH (TU 38.101524-93) – 20,8 thousand tons/year
• Natural stable gasoline (TU 39-1340-89) – 47 thousand tons/year
“Surgutneftegas” OAO
52
Since the beginning of the 1970s LENNIIHIMMASH Group has been carrying out a complex of works for the development of gas processing units for the Orenburg Helium Plant (OHP).
OHP units are unique because nowhere in the world helium is recovered from “lean” gases (content of helium is 0.055 %).
Helium extraction factor is 97-99%.
Ethane extraction factor is 60%.
In 2006 LENNIIHIMMASH Group completed reconstruction of helium unit No2 intended to increase ethane extraction and to exclude helium extraction.
Ethane extraction factor is 95%.
“Orenburggazprom” LLC
53
LENNIIHIMMASH Group completed the following works associated with Helium plant phases I, II, III revamping, including obtaining expert approval:
1. Detailed design for revamping of helium units at phases I, II, III of the Orenburg Helium Plant
2. Technical inspection of the units equipment.
3. Expert review and approval of process procedures for the units and facilities of the Orenburg Helium Plant
4. Research works, thermotechnical calculations.
“Orenburggazprom” LLC
Composition of the recovered helium concentrate:
Composition, % mol.
Helium concentrate
Не 85
N2 15
СН4 traces
Phase I – two helium units (HU No1 and HU No2) with total capacity of 6 billion m ³ / year of the processed gas.
Phase II – three units for recovery of helium concentrate
(facilities 410, 420 and 430), ethane fraction and WFLH with total capacity of 9 billion m ³ / year of the processed gas.
Phase III – one unit (U-630) with total output of 3 billion m ³ /
year of the processed gas.
Helium concentrate is recovered during step-by-step concentrating of helium in strippers with counter flow condensation as a last step.
External cooling cycles are provided in the units, including propane cycle with two isotherms of evaporation and nitrogen cycle.
Commercial helium is extracted at the fine helium purification units.
54
Year Name of project
2016 Feasibility study “Basic process solutions and options for construction of liquid natural gas production plant in Arkhangelsk oblast, including the study of its possible locations”
2013-2014 Technical and process analysis of solutions on liquefied natural gas production at a helium plant. Capacity 500 – 2 000 kg/h
2013 Report “Technical proposal for packaged equipment supply for large capacity LNG production unit using local technology and equipment” (Phase 2). Capacity 4.8 mln. t/year; capacity 1.3 mln. t/year
2013 Report “Technical proposal for package supply of experimental-industrial LNG production unit using local technology and equipment “ (Phase 1). Capacity of LNG 125 kg/h
2012 Feasibility study “Analysis of options for expansion and revamping of Yakutsk GPP”, which has LNG extraction unit as its part
2005 Feasibility study «Substantiating technology for liquefaction and storage of natural gas exported from Ust-Luga port». Liquefied petroleum gases (LPG) transshipmencomplex in Ust-Luga trading sea port. Process units and structures. Isothermic storage park. Feasibility considerations for «SIBUR – Portenergo» LLC.
1986 Low-temperature natural gas liquefaction unit with the capacity of 40 tons/h (960 tons/day)
1977 Natural gas liquefaction unit with the capacity of 20 tons/h for peak gas consumption demand in Abovyan, Armenia.
1975 Natural gas liquefaction unit with the capacity of 250 m3/h for the VNIIGAZ Experimental plant
Works of LENNIIHIMMASH Group related to LNG recovery
55
Management and execution of projects
Services in the field of engineering
Development and coordination with the Customer:
• Technical design assignment
• Engineering design
• Adaptation of design solutions of foreign engineering companies to
capabilities of Russian machine building plants and current research
and development infrastructure.
• Combination of design (Project) stage and equipment
manufacturing.
• Equipment manufacturing at leading branch enterprises.
• Engineering services in equipment manufacturing:
• Competition procedures support; placing orders for equipment
manufacturing;
• Inspections (on a rotational or permanent basis);
• Permit issuance in compliance with current laws of the Russian
Federation;
• Issuing release for shipment;
• Development of the most effective logistic scheme.
• Equipment installation on the Customer’s site.
• Commissioning works
• Performance of construction and installation works with final
"turnkey" delivery of the operating facility to the Customer.
Technical personnel in management and execution of
projects
4 Onsite representatives
6 Commissioning experts
20 Designers
4 Logistics
6 Manufacturing inspectors
6 Experts in materials
4 Experts in electric equipment
5 Experts in instrumentation
6 Experts in static equipment
4 Experts in rotating equipment
5 Executive Heads
57
Block and modular supply
• LENNIIHIMMASH Group supplies various process equipment for processing of NG and APG including block and modular supply
• Machine compressor and turbo expander equipment with capacity from 50 million m3/year to 3.0 billion m3/year is delivered in LNHM-developed block-and-modular units equipped with all necessary auxiliary and protection systems as well as lifting equipment
• Pumping, vessel, heat-exchanging, separation equipment, etc., as well as separate parts of large process lines are supplied in modules with dimensions suitable for railway transportation
Modular supply allows the Customer to reduce:
- construction and installation time;
- scope of welding at the facility;
- commissioning time;
- storage areas for the period of installation and construction;
- errors and incompliances in the documents;
- process equipment shutdown time.
58
In 2005 - 2007 LENNIIHIMMASH Group executed a project of design and delivery of process equipment for Kazanorgsintez OAO (the city of Kazan). The engineering designs were developed and approximately 500 units of non-standard process equipment were supplied for Bisfenol-A, Polycarbonates, Low-pressure Polyethylene and Ethylene plants.
“Kazanorgsintez” OAO
59
APG booster compressor station with turbine supercharger manufactured by SOLAR
TURBINES (USA) based on MARS 100S gas turbine drive
Q =16.645 / 3.991 m3/hour weight of 92 tons
60
“Noyabrsky GPC” OAO Vyngapurovsky GPP
DSG (dry gas) booster compressor station with turbine supercharger manufactured by SOLAR TURBINES (USA) based on
MARS 100S gas turbine drive Q =9.734 / 3.805 m3/hour
weight of 79 tons
61
Block-and-modular turbo expander unit
Turbo expander unit L.A. Turbine Q = 65 thousand std. m3/hour
Weight of 13,6 tons
“Noyabrsky GPC” OAO Vyngapurovsky GPP
Name of project
Number of pieces of equipment,
dimensions L*B*H (mm), weight
(kg)
Total weight
(tons) Year
“Kazanorgsintez “ OAO . Supply of equipment for the following: the Bisfenol-A plant, the Polycarbonate plant,
the reconstructed Ethylene plant, the “Low pressure polyethylene” plant
319 56 000*5 000*5 000
75 000 8 353 2005-2006
“Severorgsintez “ ZAO. Supply of equipment for “UPBS-100” gas processing unit.
117 36 000*3 200*3 200
38 000 2 323 2007-2008
“Usolye-Sibirsky Silikon” LLC. Supply of equipment for industrial production facilities of polycrystalline silicon
with the capacity of 300 tons a year.
11 13 300*2 800*2 800
18 000 366 2007-2008
“KINEF” LLC. Supply of equipment – routine maintenance.
166 59 800*3 200*3 200
58 000 2 837 2007-2009
“Gubkinsky GPC” OAO. Supply of equipment for the gas processing unit at the industrial site.
38 38 600*3 500*3 500
48 900 1 038
2009
Supply of equipment for Vyngapurovsky GPP. 150
42 000*3 500*3 500 62 400
More than 2 000 2011-2012
Supply of equipment for Yuzhno-Balyksky GPC
150 35 000*3 500*3 500
75 000 More than 1 500 2011-2012
Supply of equipment for LUKOIL- Permneftegazpererabotka
250 24 000*4 000*4 000
75 000 More than 3 000 2012 –2014
Supply of equipment for expansion of Vyngapurovsky GPP. Construction of GPU No. 2
240 (not including valves 3400 pcs) 42 000*4 500*4 700
65 000
More than 25 000
(including materials) 2013 –2015
Weight and dimensions of the supplied equipment
62
Construction Management
• Planning (development of project schedule and budget);
• Timely performance within the approved budget and in compliance with the Customer’s
quality requirements;
• Control and acceptance of installation and construction works;
• Technical supervision of construction/revamping and commissioning works;
• Coordination of subcontracting works;
• Acceptance, quality control of delivered materials, structures and equipment;
• Planning, procurement, control of construction and installation works;
• HSE control;
• Organization of management personnel training, instructing site personnel;
• Preparation for commissioning and start-up: pre-commissioning of the main process
equipment, commissioning of the whole facility with reaching design performance
(including development and coordination with the Customer: commissioning
programme, work procedures, scheduled plan with due consideration of timing of
construction and installation works etc.), as well as development of operational
documentation (emergency response plan, process procedures, operating and
maintenance manual etc.).
63
Research and development
Dehydration
Patent No. 2296793 dd 08.04.2005
“Pre-transport hydrocarbon gas treatment unit"
65
Development of the adsorber internal design
Analysis of the distributing device operation to provide for uniform speed of the inlet adsorber gas and minimum pressure loss.
66
Patent No 2530112 dd 10.08.2012
“Vertical adsorber with fixed-bed adsorbent”
Gas Separation and Gas Fractionation
Patent No 2225971 dd 03.03.2003 “Associated Petroleum Gas Separation Method"
67
source gas
stripped gas
APB Propane fraction
Deethanized Condensate
natural stable gasoline
Butane fraction
Contacts
19, Uralskaya str., bld. 5, letter D,
St. Petersburg, Russia, 199155
Telephone:
(812) 327-7960
Fax:
(812) 327-7692
We believe our experience and knowledge will contribute to your future projects!
68
Attachment: List of References
LENNIIHIMMASH Group
The List of major projects executed by LENNIIHIMMASH Group
•1997 – development of project design and detailed design documentation and supply of the main process equipment for “UPBS-3” unit at Shurtan field (Uzbekistan) with the capacity of 3.0 billion m3 (receiving propane butane technical and stabilized condensate).
•2005 – development of a detailed design for reconstruction of the phase 1 helium unit at the Orenburg helium plant to increase ethane recovery up to 95%.
•2003-2005 – development of project design and detailed design documentation, process procedures for the APG processing plant “UPG-3” at Surgutneftegas OAO with the capacity of 3.0 billion m3/year receiving PB mixture, WFLH and NSG (natural stable gasoline). Start-up of the unit – July, 2006. Target component recovery factor- 98.5%.
•2005-2007 – Reconstruction of production and processing plants of low pressure polyethylene, ethylene and construction of the Bisfenol-A and Polycarbonate plants. The equipment was supplied to the following plants of Kazanorgsintez OAO: “Low Pressure Polyethylene”, "Bisfenol-A", "Polycarbonate", "Ethylene". The unique licensed equipment was designed, manufactured and supplied in compliance with ASME standards adapted to the existing Russian standards and requirements to specifications and technical documentation. Total of 500 pieces of equipment were supplied (heat exchangers, vessel equipment, air coolers, columns, reactors).
70
• 2005-2006 – development of the design and detailed design documentation of Sayansk helium plant Sayanskkhimplast (TNK-BP) with a capacity of 2.5-4.0 billion m3/year for initial gas with release of helium.
• 2008 - development of the design and detailed design documentation and operating procedures of the full-profile plant for Severorgsintez ZAO in Novy Urengoy, including gas processing facility with capacity of 1.21 billion m3/year and 252 thousand tons per year of unstabilized condensate (with PB mixture recovery and stabilized condensate recovery). Main process equipment, valves, DCS of technological process, instruments were delivered. Coefficient of extraction of target products is 94.6%. The commodity park was constructed as part of the project under the EP contract.
• 2008 - Development of the design and detailed design documentation, development of engineering designs of processing equipment of the commodity park (8 spherical tanks, each of 600 m3), receipt, storage and shipment of the liquefied petroleum gases (LPG) for UPBS-100 gas processing complex of Severorgsintez ZAO in Novy Urengoy. Processing equipment, including tanks of commodity park, as well as fittings, DCS of technological process and instruments were delivered. The commodity park was constructed as part of the project under the EP contract.
• 2008 – development of the detailed design documentation for stages 3 and 4, as well as operating procedures for Shurtan GPP in Uzbekistan with application of the advanced technology with capacity of 3.0 billion m3/year for initial gas with PB mixture recovery. Start-up of two stages was in 2008.
• 2008 – development of the design and detailed design documentation for chlorsilane condensation units and polycrystalline silicon production units with capacity up to 3 000 tons. Main processing equipment, valves and instruments were delivered. Usolye-Sibirsky Silikon, LLC.
71
• 2009-2010 – development of the design and detailed design documentation for construction of the new production facility of Gubkinsky GPC (SiburTyumenGaz OAO ) with capacity of 2.0 billion m3/year for initial gas with recovery of WFLH. Development of operating procedures. Main processing equipment, valves, DCS, instruments were delivered. Start-up of the facility was in October, 2010. Coefficient of extraction of target products is 99.5%.
• 2010-2012 – development of the design and detailed design documentation for construction of the new production facility at Southern Balyk GPP (SiburTyumenGaz OAO ) for processing of 2.0 billion m3 of gas per annum with the recovery of ethanized WFLH. All processing equipment and materials above ground level were delivered. Coefficient of extraction of target products is 99.5% under the project of increased recovery of WFLH at Southern Balyk GPK. Start-up of the facility was in September, 2012.
• 2010-2012 – development of the design and detailed design documentation for construction of Vyngapurovsky GPP (SiburTyumenGaz OAO ) with capacity of 2.4 billion m3/year with recovery of the ethanized WFLH. All processing equipment and materials above ground level were delivered. The contract provides for a guarantee to achieve the required quantity and quality indicators of products. Coefficient of extraction of target products is 99.5%. Start-up of the facility was in December, 2012.
• 2011-2012 – development of the design documentation for construction of the condensate stabilizer within the East Urengoy license block with capacity of 5.5 million tons/year for ZAO «ROSPAN INTERNATIONAL» (TNK-BP Holding OAO ). The expert approval of "Glavgosekspertiza of Russia" was obtained. 72
• 2011-2012 – development of the design documentation for construction of the gas cooling station with capacity of 15 billion std. m3/year and deethanization compressor plant within the East Urengoy license block with capacity of 900 million std. m3/year for ROSPAN INTERNATIONAL ZAO (TNK-BP Holding OAO ). The expert approval of "Glavgosekspertiza of Russia" was obtained.
• 2013-2014 – development of the design documentation for “Reconstruction of APG treatment plant at GPP of Langepasneftegaz at LUKOIL-Western Siberia OAO ” as well as for reconstruction of the commodity park with the loading rack of Lokosovsky GPP for processing of 2.1 billion m3/year of APG with the recovery of 1.46 billion m3/year of dry gas, 742.4 thousand tons/year of WFLH, 122.4 thousand tons/year of natural stable gasoline, 4.2 thousand tons/year of propane. WFLH product pipeline DN250, PN 4.0 MPa with the length of 16 km.
• 2011-2014 – development of technological process, development of design documentation (obtaining approval of Glavgosexpertiza of Russia), development of detailed design documentation for construction of the 2nd processing stage with capacity 1 bln. m3/year of APG and 512 thousand tons/a year of WFLH (including compressor stations, columns, dehydration unit with gas fractionation unit, odorization unit, refrigeration cycle compressor station, outdoor low temperature condensation and rectification unit, petroleum gas compressor station etc.) for LUKOIL-Permneftegaspererabotka OAO . Main technological equipment was supplied, valves, DCS, instrumentation. Author’s supervision over construction was performed, as well as supervised installation of the equipment and commissioning works. Target components extraction coefficient – 99.4%.
73
• 2013-2015 – development of technological process, development of design documentation (obtaining approval of Glavgosexpertiza of Russia), development of detailed design documentation for construction of new processing line with capacity 1.4 bln. m3/year of APG at Vyngapurovsky GPP (including preliminary separation unit, compressor stations, dehydration unit, furnaces unit, low temperature condensation and rectification unit, turbo expanding unit, methanol injection unit, fuel gas treatment unit, heat transmission unit etc.) for SiburTyumenGaz ОАО . All the process equipment was supplied, as well as all the utility systems and materials above and below “zero”, valves, DCS and instrumentation. The following services were rendered: author’s supervision over construction, supervised installation of the equipment. Commissioning works were performed. Target components extraction coefficient – 99.5%.
• 2017 – Shurtanneftegaz LLC Development of the basic design package, including feasibility study
for incresing of market product output of the units of UPBS-3 (for stages 1, 2 and 5).
• 2016-2017 – Development of main technical solutions and design documentation for tie-in of new 4-cell ethane cracking furnace P-810/815/820/825 as part of ethane and propane fractions pyrolysis station in tube furnaces at the operating E-200 unit of Ethylene plant of PAO “Kazanorgsintez".
• 2018 – Supply of (on the basis of technical detailed designs developed by own manpower) pressure reduction and steam cooling units ROU-801...804, tank Е-835 and heat exchanger Т-804, receiver block Е-801, filter Ф-802/А, Б and atmospheric deaerator Е-802 for completing the Ethylene plant of PAO “Kazanorgsintez” as part of works on reconstruction of the cracking furnaces.
74
List of the main feasibility study reports made by LENNIIHIMMASH
Group
• 2005 – SIBUR-Portenergo, LLC. Feasibility analysis of liquefaction and storage of natural gas subject
to export from Ust-Luga port. Liquefied petroleum gases (LPG) handling system in the sea trade
port of Ust-Luga. Process units and structures. Isothermal storage. Feasibility study.
• 2005 – Study of possible options of processing of Karachaganaksky gas at Phase 1 reconstructed
units of Helium Plant of Orenburggazprom, LLC.
• 2006 – Kazoil, LLC. Investment Feasibility analysis of construction project “Utilization of associated
petroleum gas of Alibekmol and Kozhasay fields”.
• 2006 – "ZEROMAX GMBH" Switzerland. The preliminary feasibility study of construction of two
recovery units of propane, butane and their mixtures from raw materials of Shurtan Group fields.
• 2007 –SiburTyumenGaz OAO . Revamping of NTK UPG-2 unit of Gubkinsky GPC. Feasibility study.
• 2007 –VAO AgroKhimEksport ZAO . Investment feasibility analysis of methanol producing plant
with capacity of 500 thousand tons per annum.
• 2007 –PROMGAZ OAO . Feasibility analysis of helium extraction in hydrocarbon helium bearing
fields in Eastern Siberia and the Republic of SAKHA (Yakutia).
75
• 2008 –SiburTyumenGaz OAO . Analysis of design solutions for retrofit of “UPG-1” of Yuzhno- Balyksky GPC".
• 2009 –PROMGAZ OAO . Basis design development for calculation of performance indicators of gas processing facilities in the gas fields of Irkutsk Oblast. Gas processing plant with helium recovery in Ust Kut.
• 2009 –PROMGAZ OAO . Basis design development for calculation of performance indicators of gas processing facilities. Gas processing plant in Kirensk.
• 2010 –SURGUTNEFTEGAS OAO . Development of process options for APG treatment systems at gas-fueled reciprocating power plants.
• 2010 – Gazprom VNIIGAZ, LLC. Investment feasibility analysis of “Market Helium Production” as part of the investment program for arrangement and transportation of hydrocarbons of Sobinskoye oil and gas field.
• 2010 –TOMSKNIPINEFT OAO. Helium production methods within the project of “Development of NK Rosneft OAOstrategy to enhance Helium Industry in the helium fields of Eastern Siberia”.
• 2011 – OAO GAZPROM NEFT. Cost assessment in terms of transport and stabilization of condensate recovered at the license blocks of the Yamalo-Nenets Autonomous Area.
• 2011 – Feasibility study to improve the recovery rate of target components, to recover ethanized WFLH and to separate it from CO2 at JSC Belozerny GPC and JSC Nizhnevartovsk Gas Processing Complex. YUGRAGAZPERERABOTKA, LLC.
76
• 2011 – TNK-BP Management, LLC. Feasibility analysis for “Market products demethanolization units" at the condensate stabilizer of the East Urengoy license block.
• 2011 – FBK, LLC. Feasibility study “Construction of ethane and WFLH recovery unit” for Gazprom Dobycha Orenburg, LLC with gas processing capacity of 6.9 and 15 billion m3/year.
• 2011-2012 – LUKOIL – Western Siberia, LLC. Process design and feasibility study of reconstruction options for Lokosovsky GPP.
• 2011-2012 –Sakhatransneftegaz OAO . Feasibility analysis “Yakut GPP expansion and revamp options”.
• 2012-2013 – Feasibility analysis for “Reconstruction of gas fractionation plant with development of infrastructure for raw material discharge, storage and shipment of market products at workshop of Sibur Khimprom ZAO .
• 2012-2013 – Feasibility analysis for “Expansion of Vyngapurovsky GPP. Construction of gas processing unit (GPU-2) of SiburTyumenGaz OAO .
• 2012-2013 – Feasibility analysis for Gazprom VNIIGAZ, LLC. "Technical proposal for supply of the complete set of LNG production unit using domestic technology and equipment”.
• 2013 – Gazprom pererabotka, LLC. Expert assessment of the design solutions for low pressure waste gas disposal unit at Surgut Condensate Stabilization Plant.
• 2014 – Gazprom Dobycha Orenburg, LLC. Feasibility study of the project of LNG production at helium plant.
• 2014 – TOBOLSK-NEFTEKHIM, LLC. Feasibility study of “Construction of propane-propylene fraction recovery unit supplied with off-gas feed”.
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• 2014 –FORTUM OAO . Main design solutions "Construction of Gas Processing Plant near the city of Nyagan”.
• 2014 –Yamal-Povolzhye OAO . Project of GPP for ethane and WFLH production in Yambursky and East Urengoy fields.
• 2014 –AK ALROSA OAO . Selection of the best option of the Concept allowing for the maximum replacement of liquid motor fuel by natural gas with the smallest investment risks and costs and within the shortest possible time limits.
• 2015 – SiburTyumenGaz OAO Feasibility analysis of replacement of P-1 furnace by the recuperative heat exchanger at the Gas processing unit No. 2 (low-temperature condensation unit and external equipment). Reconstruction at the industrial site of Gubkinsky GPP.
• 2015 – SiburTyumenGaz OAO . Belozerny GPC, LLC. Main design solutions for Reconstruction of Bakhilovsky compressor station and infrastructure for transportation of APG to Belozerny GPC and Nizhnevartovsk GPP.
• 2015 - Yamal-Povolzhye PAO . Feasibility analysis for the condensate stabilization unit of the Urengoy oil and gas condensate field.
• 2015 – Nizhnekamskneftekhim PAO . Feasibility analysis of construction of light hydrocarbon fraction recovery facilities as part of Yamal-Povolzhye product pipeline construction project.
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• 2016 – Kazanorgsintez PAO . Feasibility analysis. Assessment of capital costs for construction of Gas
Processing Plant for treatment of wet gas from the Valanzhinian deposits in the Republic of Tatarstan.
• 2016 – Transportnaya Integratsiya, LLC. Feasibility analysis. Main design solutions and options of
construction of the LNG production plant in Arkhangelsk Oblast, including feasibility analysis of its
potential locations.
• 2017 – Shurtanneftegaz, LLC Development of the Basic Design Engineering, including feasibility
analysis to increase the market product yield at UPBS-3 butane-propane recovery units (phases 1, 2
and 5).
2016-2018 2017-2018
Construction of 4-cell ethane cracking furnace of«Technip Benelux B.V.» P-810/815/820/825 with
the capacity of 72 tons/hour as part of pyrolysis station of pyrolysis and gas purification shops №58-
68 of PAO “Kazanorgsintez” ethylene plant
LENNIIHIMMASH GROUP LLC performed the tie-in of the cracking furnace to the network of the plant
and designed the utility systems :
Feed and fuel gas treatment
Process nitrogen and instrument air feed system
Steam supply and condensate discharge system
Feed water conditioning system
Blow-down water system for hardness salts removal from the steam drum and boiling
sections
Off-site facilities and utilities (water supply and sewerage, office building, power supply, fire
station, central control room etc.)
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Retrofit of the water wash unit of cracking gas and interstage equipment of compressors В-401/A,B,
stage 4 of E-200 shops №58-68 and №65-76.
As part of the revamp project LENNIIHIMMASH GROUP LLC designed and delivered:
Interstage heat exchangers that are designed to allow mechanical cleaning of the shell side
Quench water air cooler that ensures the required water temperature in the middle part
of the cracking gas water washing column
As the result of the revamp even without CG compressor revamping , the capacity of the
pumpable gas was increased from 64 tons/hour to 78 tons/hour
Cooperation experience of LENNIIHIMMASH GROUP and Technip
Benelux B.V.
Attachment (PAO Kazanorgsintez)
Cooperation experience of LENNIIHIMMASH GROUP and Technip
Benelux B.V.
2017-2019
Ethylene plant propane flexibility revamp for PAO “Kazanorgsintez" Basic design development - Technip Benelux B.V. (process part)
The aim of the revamp - reaching of the plant output capacity - 605 thousand tons/year of high purity ethylene in the conditions of insufficiency of ethane feed supply
Keeping up the annual ethylene output capacity will be achieved by using propane feed (balancing feed)
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Works performed by LENNIIHIMMASH GROUP
Review of the supply of the designed facilities with utility systems:
Process nitrogen and instrument air system
Steam supply and condensate discharge system
Circulating water supply system
Flare system performance check
Chemical agents dozing system (demulsifier, PH regulator, polymerization inhibitor)
Off-site facilities and utilities (water supply and sewerage, office building, power supply, fire station, central control room etc.)
Attachment (PAO Kazanorgsintez)
Current work of LENNIIHIMMASH GROUP and Technip
Benelux B.V.
2018-2019 гг
Retrofit of the cracking furnaces F1003, F1004, F1005, F1006 of the ethylene plant for “Stavrolen” LLC
Goals:
insuring smooth operation of ethylene production cracking furnaces
achieving stability of the production processes
reducing number of the furnaces emergency shut downs
reducing time of furnaces maintenance shut downs
insuring constant furnaces reserve due to complex overhaul repairs
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Works by LENNIIHIMMASH GROUP
Review of the supply of the designed facilities with utility systems:
Development of technical designs for the revamped furnaces;
Development of detailed design documentation for the tie-in of the furnace to the existing systems (fuel gas, dilution steam);
Supply of materials and equipment;
Execution of construction and installation works on the cracking furnaces;
Designer’s supervision of the construction;
Managing pre-commissioning and commissioning works;
Execution of complex furnace testing.
2017-2019
Attachment (PAO Kazanorgsintez)