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The company was incorporated in the year 1992 and has its office and manufacturing facility in Pune.

Xytel India - An Insight

The quest for bringing in “World Class Technologies” to the Indian Subcontinent & Asian Region has been a guiding force in establishing Xytel India.

Xytel India is the pioneer in bringing the Revolutionary Pilot Plant Technology to the chemical Research and Development Industry.

Xytel India, a joint venture between Xytel Corporation, USA, the world leader in supply of pilot plants & Aker Solutions (earlier Kvaerner/Davy Powergas, Mumbai), a premier project/process engineering organisation is engaged in supply of skid-mounted/modular, fully automated Pilot/Mini Plants on turnkey basis.

Xytel India - An Insight

Why Xytel India ?

Expertise in designing and building cost effective pilot and mini plants in record time, providing modularity, portability and computerised control

State-of-the-art manufacturing facility

Customer Satisfaction

Customized pilot/mini plants for specific requirements.

Prompt, Reliable & Efficient Service

Skilled and Experienced work force

Specialized overseas/ Indian vendors

Real time consultations with Xytel Inc. US for product upgradation & sharing their data bank and immense global experience

In-House Software Development Capability

Availability of Design software like ChemCAD, APV, PromisE, AutoCAD

Xytel India Methodology of Project Execution

Customer Requirement

Literature Survey, Preliminary Engineering,Finalize specification

Client

Client

Firm Order from Client

Basic Engg. Package, Process Design, Detailed Engineering, Mechanical Design & Control System Config.

Client

Procurement, Fabrication & Assembly

Factory Acceptance Test & Site Acceptance Test

Warranty Support

Client

Purpose:• For conducting simulated testing of commercial

units, for correctly estimating the yield changes

Project Details:• Operating Temperature :

Reactor : 500 – 600oC

Stripper : 500 – 600oC

Regenerator : 650 – 720oC• Operating Pressure : 2 – 5 kg/cm2 g • Feed Rate : 2 To 12 kg/hr.• Feed Type : Naphtha, VGO/Resid of CCR < 1 (wt

%)• Catalyst circulation rate : 40-100 kg/hr• Stripping Medium : Steam/Nitrogen• Adiabatic operation of the riser• PC-PLC based control system• Year of completion: 2009

Fluid Catalytic Cracking (FCC) Pilot Plant

Client: Reliance Petroleum Limited

Purpose:For conducting catalyst and process evaluation

studies

Project Details:• Feed Rate : 50-500 ml/hr• Operating temperature: 500oC max.• Operating pressure: 180kg/cm2g max.• Catalyst capacity: 150cc max.• Unit included, 5 reactor systems having

up/down flow arrangement with series & parallel arrangement.

• High Pressure Scrubber system• Atmospheric column for Top & Bottom

separation.• PC-PLC based control system• Year of completion: 2009

Dual Hydrotreater / Hydrocracker Pilot Plant

Client: Takreer, Abu Dhabi

Purpose:For deactivating zeolite based fresh FCC/RFCC

catalysts & additives without or with metals

Project Details:• Reactor MOC: Incolnel 800H• Operating temperature: 850o C• Operating pressure: Atm.• Catalyst Qty: 75 cc• Water Feed Rate: 3.6 - 25 cc/hr• Unit included: 4 reactors installed in a sand

bath, 4 feed pumps, rotameter for nitrogen and air service, Mass Flow Controller for Hydrogen

• PC-PLC based control system• Year of completion - 2012

Multireactor Fluid Bed Auto Steaming Unit

Client: Indian Oil Corporation, Faridabad

Purpose:For aviation fuel production from vegetable oil.

Project Details:• Reactor MOC: SS316• Operating temperature: 500o C• Operating pressure: 150 bar.g• Catalyst Qty: 4 litres• Liquid Feed Rate: 3-10 ltrs/hr• Gas Feed Rate : 600-6000 SLPH• Mode of Operation: Once Thru & Recycle• Micro Processor Controller based system

with feature of controlling from PC• PC-PLC based control system• Year of completion - 2012

High Pressure Fixed Bed Pilot Plant Flow Reactor System

Client: Indian Institute of Petroleum

Purpose: • Two units meant for light and heavy feeds.

Project Details:• Operating Temperature: 450oC

• Operating Pressure: 150 bar.g

• Catalyst capacity: 250 ml

• 6 Tubular Fixed Bed Reactors

• All 6 reactors can be operated in Series or 3 & 2 reactors can be operated in series independently

• Separator Section With 2 Phase Separator

• On-Line GC analysis

• PC-PLC based control System

• Year of completion : 2009

Multiple Microreactor Distillate & Residues Catalyst Testing Units

Client: Kuwait Institute of Scientific Research

(Unit A&B)

Client: Indian Oil Corporation Limited Purpose:

• For rapid evaluation of hydro-processing

catalysts.

Project Details:

• Operating Temperature:450oC max.

• Operating Pressure: 200 bar g max.

• Catalyst Capacity: 1-5 ml

• Unit included: total 8 reactors

(MOC:Inconel) installed in three zone

furnace and having separate feed, product

& separation module for each reactor with

high precision syringe feed pump for

liquid feed.

• PC-PLC based control system

• Year of completion: 2009

FULLY AUTOMATIC MICRO -REACTOR SYSTEM CONSISTING OF EIGHT REACTORS

TOLUENE DISPROPORTIONATION UNIT (HT&OT)

Client: Shanghai Research Institute of Chemical Technology (SRIPT), China

Purpose: • To study catalyst & operating conditions in 10 Independent reactor

system.

Plant Details:• Operating temperature: 400oC • Operating pressure: 40 bar g• Catalyst capacity: 25-50 cc• Reactor type: Fixed Bed Reactor

• Reactor MOC: SS316

• Liquid feed: Toluene & Cg,C10 Aromatic (feed rate: 5-200 gm/hr)

• Gas feed: Hydrogen (feed rate: 100SLPH)

• DCS based control system.• Year of completion : 2008

Client: Sabic Research & Technology Pvt Ltd

Project Details:• Operating Temp.: 800oC at atm

pressure and 600oC at 60bar.g pressure.

• Reactor of catalyst volume: 2ml • Reactor MOC: Inconel 625 (Qty. : 8

Nos.)• Gas Feed: H2, N2, Air, Hydrocarbon

gases (Methane/Propane)• Liquid feed: Hydrocarbon such as

Benzene etc.• PC-PLC Based Control System• Unit included 8 Port Stream Selection Valve arrangement and Multiport

Sampling Valve with 16 Nos. of 2ml sampling loops• Year of completion: 2006

Purpose: • Aromatic Alkylation, Alkane cracking, gas

phase dehydrogenation

MULTIPLE FIXED BED HIGH THROUGHPUT CATALYST SCREENING REACTOR SYSTEM

Client: Kuwait Institute of Scientific Research

Purpose: • Hydrotreating Of VGO For Catalyst

Evaluation.

Project Details:• Operating Temperature: 450oC

• Operating Pressure: 200 bar.g

• Catalyst capacity: 250 ml

• 5 Tubular Fixed Bed Reactors

• All 5 reactors can be operated in Series or 3 & 2 reactors can be operated in series independently

• Separator Section With 2 Phase Separator

• On-Line GC analysis

• PC-PLC based control System

DIRECT UPGRADING PILOT PLANT

Client: Indian Oil Corporation Limited

• Purpose: • Reforming of Natural Gas, Methane, Naphtha

Steam.

• To carry pre-reforming, primary reforming, HTS and MTS/LTS reactions

Project Details:• Operating Temperature: 900oC & 550oC

Operating Pressure: 50 bar.g

• Unit included: feed pre heater & steam super heater, total 5 Tubular Fixed Bed Reactors of 50cc catalyst capacity each operated independently or in series.

• Hydro de-sulfurisation, Sulfur Guard

• On-line GC Analysis

• PC-PLC based control System• Year of completion: 2004

SYN-GAS MICROREACTOR UNIT

Purpose: • For Hydrodynamic and column internal studies in the Trickle Bed Reactor

Project Details:

• Unit included two fixed beds of 600 mm dia and 1000 mm height of each bed

• Unit had different types of distributors such as bubble cap tray, sieve tray and chimney tray

• Arrangement to check efficiency of quench box

• Specially designed liquid collector with 60 equal compartments and separate measuring tube for each collector

• Column in Acrylic and internals in SS• PC-PLC based control system• Year of completion: 2005

COLD STAND UNIT

Client: Indian Oil Corporation Limited

Client: Indian Oil Corporation Limited

Purpose: • Hydrocracking of VGO for catalyst

evaluation

Project Details:• Operating Temperature: 450oC

• Operating Pressure: 200 bar.g

• VGO feed with recycle feed module

• Unit included: total 2 tubular fixed bed reactors (MOC:RA330) of 400 ml catalyst capacity, such that the reactors operate in series, parallel or independently.

• Unit also included separator section with 2 phase separator, Caustic scrubber & recycle gas compressor, liquid stripping with stripper, packed heated atmospheric & vacuum column, cast in Bronze block furnace and LPG recovery system.

• PC-PLC based control System• Year of completion: 2005

HYDROCRACKER PILOT PLANT UNIT (FIXED BED

Purpose:• For conducting simulation of

catalyst deactivation for evaluation of fresh catalyst.

Plant Details:

Client: Chennai Petroleum Corporation Limited (Formerly MRL)

• Operating temperature: 900oC • Operating pressure: atm.• Catalyst capacity: 100 gm.• Reactor type: Fluidized Bed

Reactor • Reactor MOC: Incolly 800 • Liquid feed: VGO (feed rate: 5-

25gm/min; preheat temp.: 350oC)• Gas feed: Air/ Nitrogen (feed rate:

500SCCM; preheat temp.: 350oC)• PC-PLC based control system.

CYCLIC DEACTIVATION UNIT

Purpose:

• For adsorption of Sulfur in packed/fluidized bed of adsorbent.

• In-situ activation & regeneration of adsorbent.

Plant Details:

• Adsorber MOC: RA-330

• Operating temperature: 550oC,

• Operating pressure: 30 bar.g

• PC-PLC based control System

• Year of completion: 2004

Client: Indian Institute of Petroleum

LAB-SCALE ADSORPTION UNIT FOR GASOLINE DESULPHURISATION PLANT

Client: Kuwait Institute of Scientific Research

Purpose:

• Two units meant for light and heavy

feeds.

Project Details:

• Operating Temperature: 450oC

• Operating Pressure: 150 bar.g

• Catalyst capacity: 5 - 10 cc

• Multiple reactors in single furnace

• PC-PLC based control System

• Year of completion: 2005

MULTIPLE MICROREACTOR DISTILLATE AND RESIDUES CATALYST TESTING UNIT-A & UNIT-B

Client: Indian Oil Corporation Limited

Purpose: • Reforming of Natural Gas, Methane,

Naphtha Steam.

• To carry pre-reforming, primary reforming, HTS and MTS/LTS reactions

Project Details:• Operating Temperature: 900oC &

550oC Operating Pressure: 50 bar.g

• Unit included: total 5 tubular fixed bed reactors of 100cc catalyst capacity each operated independently or in series, steam super heater, online GC analyzer.

• Hydro de-sulfurisation, Sulfur Guard

• PC-PLC based control System

• Year of completion: 2004

HYDROGEN GENERATION UNIT

Client: Bharat Petroleum Corporation Limited

Purpose: • For studies of isomerisation &

reforming processes of Naphtha

Project Details:• Operating Temperature: 550oC• Operating Pressure: 50 bar.g• Reactor catalyst capacity: 20cc • Fixed bed reactor system, with

up/down flow arrangement.• Plant included Hydrogen recycle

system

• Unit included on-line CO/CO2

analyzer• PC-PLC based control System

• Year of project completion: 2003

REFORMING MICRO REACTOR PILOT PLANT

Client: Bharat Petroleum Corporation Limited

STEAM DEACTIVATION UNIT

Purpose:• Designed to decrease the activity

of fresh FCC Zeolite catalysts by processing it for a period of time in presence of steam at 750 – 800oC.

• To simulate fully equilibrated FCC catalyst conditions after deactivating the catalyst.

Plant Details:

• Operating temperature: 400oC • Operating pressure: atm.• Catalyst capacity: 50-100 gm/min• Liquid feed rate: 5-25 gm/min

(VGO/Resid)• Gas feed rate: 200 SCCM (Air/

Nitrogen)• PC-PLC based control system

Purpose:• Cracking of Ethane

• To study the effect of anticoking agent on coking in the tubular reactor

Project Details:• Operating Temp.: 830oC (max.)• Operating Pressure: 2.5 bar.g• Capacity - 5 kg/hr Ethane Gas• Process design was done by IICT,

Hyderabad.

Client: Gas Authority India Limited

• The reactor was incorporated with gas fired furnace using metal fibre (Acotech, Belgium) and water cooled gas burners

• PC-PLC based control system.• Year of completion: 2001

GAS CRACKER PILOT PLANT

Client: Indian Petrochemical Corporation Limited

DEHYDROGENATION CATALYST TESTING UNIT

Purpose:• For catalytic screening/kinetic

studies for dehydrogenation reactions.

Plant Details:

• Operating temperature: 500oC • Operating pressure: 50 bar.g.• Catalyst capacity: 2-5 ml.• Liquid feed rate: 3-90ml/hr.• Hydrogen recycle capability using

compressor.• System included, fixed bed tubular reactor in downflow arrangement, HP make 6890 series Gas Chromatograph & HPLC type syringe pump for

water addition.• PC-PLC based control system.• Year of completion: 2000

Client: Indian Oil Corporation Limited

Purpose:• For cracking of heavier feeds with CCR to 12

wt% max.• For studying FCC catalyst properties, dual

solid process and integral regenerator/reactor system

• For feedstock and catalyst evaluation.

Project Details:• Design pressure: 2 bar.g• Feed rate: 4 - 10 kg/hr• Two stage regeneration operation at 700-750oC • Adiabatic operation for reactor & regenerators• Debutaniser @ -20oc• Online CO/CO2/O2 analysis of flue gas

• Steam generation facility for feed injection & Hydrocarbon Stripping• Internal/external cyclones in regenerator.• Online product and flue gas flow rate measurements.• Proprietary feed nozzle design by Xytel India• PC-PLC based control System• Year of project completion: 2001

RESID FCC PILOT PLANT

Purpose:

• Determination of characteristics of a particular Fluid Cracking Catalyst.

Plant Details:

Client: Chennai Petroleum Corporation Limited (Formerly MRL)

• Reaction Temp. : 550oC • Regeneration Temp. : 750oC• Liquid Product Collection : Icebath• Feed Injection Rate : 0.5 to 60 ml/min• Feed Syringe Temp. : 100oC• Reactor Capacity :4-5 gm of catalyst• Nitrogen Flow Rate : 100 cc/min max.• PC-PLC based control system.• Year of Completion : 1996

MICRO ACTIVITY TEST UNIT

Client: Kochi Refineries Limited

Purpose: • To study effect of reaction/

regeneration temp.

• To study catalyst circulation rate.

• Feedstock on FCC process.

• Catalyst/feed stock comparison

Project Details:• Operating Temperature: 600-750oC

• Operating Pressure: 2.7 bar.g

• 7.5 kg/hr catalyst circulation rate

• 2.5 kg/hr liquid feed rate

• PC-PLC based control System• Year of completion: 1996

FLUID CATALYTIC CRACKING PILOT PLANT

Client: Indian Oil Corporation Limited

Project Details:• Operating Temperature :

Reactor : 45 – 510oC

Stripper : 500 – 550oC

Regenerator : 650 – 750oC

• Operating Pressure : 0.3 - 1.5 bar.g

• Feed Rate : 0.8 To 3.5 kg/hr.

• Feed Type : VGO, VGO + Resid of CCR < 1 (wt%)

• Catalyst circulation rate : 6-10 kg/hr

• Recycle Ratio < 10%

• Stripping Medium : Steam/Nitrogen

• Adiabatic operation of the riser

RECYCLE FCC PILOT PLANT

• Unit included: CLO column, HGO column & debutaniser at the down stream of reactor and online CO/CO2/O2 analyzers for flue gas

• PC-PLC based control system

Purpose:• For selective Hydrogenation, Hydro de-

sulfurization, Hydro dewaxing & Hydro cracking

• For catalyst screening, their performance evaluation & comparison and to extract the kinetic data

Project Details:• Design temperature: 550oC• Design pressure: 200 bar.g• Reactor catalyst capacity: 150cc and

20cc for MCR.• Plant included Hydrogen Recycle Facility

Client: Indian Oil Corporation Limited

• Unit included: two reactor system with up/down flow mode with series and

parallel arrangement with on-line GC for product gas analysis• PC-PLC based control system• Year of project completion: 2002

PILOT PLANT & MICRO REACTOR FOR MIDDLE DISTILLATE DEWAXING

Client: Kuwait Institute of Scientific Research

Purpose: • Isomerisation and hydrotreating of

hydrocarbon or naphtha gas oil cuts

Project Details:• Operating Temperature: 450oC

• Operating Pressure: 100 bar.g

• Cast In Bronze Block Furnace

• On-Line GC analysis

• PC-PLC based control System

• MOC : SS316

ISOMERISATION PILOT PLANT

Client: Chennai Petrochemical Corporation Ltd

HYDROTREATING PILOT PLANT

Purpose:• For selective hydrogeneration,

hydro- desulferisation, hydro-dewaxing, hydro-finishing & hydrocracking for catalytic screening, performance comparison & kinetic data.

Plant Details:

• Operating temperature: 550oC • Operating pressure: 250 bar.g. • Catalyst capacity: 500cc• Unit included, 2 reactor system

having up/down flow arrangement with series & parallel arrangement.

• PC-PLC based control system• Year of completion: 1998

Client: Indian Oil Corporation Limited, Faridabad

Adsorption Micro Reactor Unit

Purpose:• For carrying out research activities in the

area of catalytic/non-catalytic adsorption processes (for sulfur adsorption)

• For evaluation of different adsorbent systems, feed stocks and for optimization of process parameters

• Reactor MOC: Inconel 800• Operating temperature: 600°C• Operating pressure: 50 bar. g • Catalyst Qty : 40 cc• Liquid Feed Rate :100 ml/hr; Hydrogen Feed Rate :150 SCCM; Air Feed Rate :150 SCCM• Unit included: two reactor system with down flow mode with parallel arrangement and

sequence operation philosophy with on-line liquid and gas analysers, on-line Antek make sulfur analyser, on-line gas analyser (CO, CO2, SO2, O2)

• PC-PLC based control System• Year of completion: 2010

Project Details:

Client: Indian Oil Corporation Limited, Faridabad

Demetallation Reactor Unit

Purpose:• For development of Demetallation

process for the removal of heavy metals (Ni, V, Fe etc.) from heavy hydrocarbon oils

• Operating temperature: 260 °C• Operating Pressure: 85 bar.g• Operating pressure: 50 bar. g

• Unit included: High Pressure CSTR Reactor of 1 litre capacity with electrodes (SS/Copper/Aluminium) insertion arrangement and current control facility

• Reactor MOC : C-276 Hastealloy• Micro PLC based Control System• Year of completion: 2010

Project Details:

Client: Porocel Adsorbents, Catalysts & Services

Claus Catalyst Test Rig

Purpose:• Catalyst Activity Testing

(Catalyst developed for Sulphur production)

• Operating temperature: 380°C at Atm Pressure

• Reactor of catalyst volume: 100 ml• Reactor MOC : Quartz

• Gas feed H2S, SO2, Nitrogen, Air, CO2

• Liquid feed CS2 and Water

• Reactor, Condenser Coil, Seal Pot• MOC: Glass, Installed in oven• PC-PLC based computer systems• Year of completion: 2010

Project Details:

Client: Indian Oil Corporation Limited, Faridabad

Compact Steam Methane Reformer Pilot Plant

Purpose:• For producing HCNG mixture for auto

fuel purpose (80% methane. 20% Hydrogen)

• Producing and storing HCNG

• Reactor MOC: SS 321• Operating temperature: 500°C• Operating pressure: 10 bar. g• Steam Feed Rate: 2.5 kg/hr; CNG Feed Rate: 2 NM 3/Hr

• Unit included: Sulphur Guard reactor to remove H2S from CNG, Steam Generator & Steam super heater, CO2 Scrubber, HCNG Gas Compressor with Discharge Pressure 250 kg/cm2, HCNG Storage consisting of 7 cylinders of 75 litre capacity each, online analysers for methane, hydrogen and CO2

• PC-PLC based control systems• Year of completion: 2011

Project Details:

Xytel India Services

Feasibility & Engineering StudiesApart from the main activity, we also undertake, as a pre-requisite for turnkey supply, a study to prepare pre-engineering document to convert bench / lab-scale data to into pilot / mini plant design when very little information about the process is available. This exercise is also useful for estimating the project cost enabling the client to arrive at an investment decision.

Revamping Existing Units

Xytel India offers specialized services to help clients revamp their existing pilot plant resources.

AMC Services

Xytel India also undertake Annual Maintenance Contracts for Pilot/ Mini Plants . Each AMC has a designated service engineer in lead role and services will include visits at a mutually decided frequency, normal & preventive maintenance operations, guidance & training for proper operation & maintenance of pilot plants.

Automation of Pilot Plants

Xytel India offers solution to PC/PLC based system to replace existing, stand alone control systems, PC based control systems.

Clients

Office & Works: EL-31/14, ‘J’ Block, MIDC, Bhosari, Pune – 411026. Maharashtra (INDIA)

Tel : +91 20 40737700 Fax : +91 20 40737777Email: [email protected] Website: www.xytelindia.com

Xytel India Pvt. Ltd.