- 1. BARAUNI REFINERY INDIAN OIL CORPORATION Barauni (Bihar)(i)
Unit Profile Barauni Refinery is the second Public Sector Refinery
of Indian Oil Corporation built in collaboration with erstwhile
USSR and limited participation of Romania. It is located near the
northern bank of river Ganga in Begusarai district of Bihar. The
refinery went on stream in the year1964and wasformally inaugurated
by Prof. Humayun Kabir, the then UnionMinister for Petroleum &
Chemicals, Govt.of India on15th January,1965. The installed
capacity of crude oil processing has been enhanced from 3.3 MMTPA
to 6.0 MMTPA since Jan2003 after commissioning of process units
like RFCCU, DHDT, HGU, SRU, ARU & SWS.During the year 2003-04,
Barauni Refinery processed 4.3 MMTPA crude oil. The
differentpetroleum products produced by Barauni Refinery are LPG,
Naphtha, Motor spirit, SuperiorKerosene Oil, High Speed Diesel,
Light Diesel Oil, Raw Petroleum Coke & Sulphur.Barauni Refinery
caters to the Oil requirement of large number of customers of
Northern WestBengal, Bihar, Nepal and part of U .P.Barauni Refinery
In harmony with nature
2. 20 (ii) Energy Consumption :Refining of crude oil being an
energy intensive activity, the major chunk of expense in theprocess
is the energy cost. Therefore, the need of energy conservation is
of utmost importance.This leads to not only increase in
profitability in the form of lower energy cost and adding on tothe
bottom line but also protection of environment and quality of life.
Due efforts were made bythe refinery and various energy
conservation measures like yield and energy optimisation
ofdistillation units (AVU-I, II & III) & Coker-A &
installation of high efficiency Gas Turbine. Oldconventional
pneumatic systems used for operational controls have also been
replaced withDistributed Control System in all process units and
OM&S. These measures along with day today monitoring of fuel
& loss helped to bring down the energy consumption level from
171MBTU/BBL/NRGF in 1990-91 to 133.8 in the year
2003-04.UNIT2001-02 2002-03 2003-04 CRUDEMMT 2.91 2.99 4.30 COKER
TPUTMMT 0.67 0.65 0.45 RFCCUMMT -0.50 1.02 DHDT MMT -0.71 2.17
HGUMMT -0.04 0.92 PROCESSING COST RS / MT OF CRUDE FUEL & LOSS%
6.99 11.4*10.2 NRGF 2.85363.8312 3.8636 MBTU/BBL/NRGF 135.4146.09
133.8* Includes 1.25 % F&L towards BXP units(RFCCU / DHDT / HGU
/ SRU / ARU / AWS)commissioning.Barauni Refinery In harmony with
nature 3. ENERGY + LOSS PERFORMANCE ENERGY COST (MBTU / BBL /
NRGF)(% OF MANUFACTURING COST) 150 45146.09 39.6 145 4038.3 140
35135.4 135 133.8 30 26.9 130 25 125 20 01-02 02-0303-0401-02 02-03
03-0420 (iii) Energy Conservation Commitment, Policy and Set Up :To
conserve energy, optimisation of the operation of the process
heaters and boilers andmaximum possible heat recovery from out
going streams have been given utmost emphasis inday-to-day refinery
operations. The efficient usage of utilities, optimisation of
steam-powerbalance, and optimization of heat exchanger train have
been the prime concern in the EnergyConservation area.As a broad
classification the energy conservation activities have been grouped
under long termand short term ones. The long-term activities are
the high investment projects spread over along period. The
short-term measures consist of continuous efforts for energy
optimisation.The specific energy consumption is monitored
daily/weekly/monthly for effective control. Theoptimisation of
process conditions and implementation of energy conservation scheme
is giventhe highest priority.Energy Conservation fortnight is
celebrated every year from 15th Jan to 31st January.
Variouscompletion like essay, slogan, poster on energy saving and
cycle rally & in-house seminar isconducted. Barauni Refinery In
harmony with nature 4. The importance of energy conservation is
emphasized through TPM (Total ProductiveMaintenance) by achieving
zero breakdown, zero defect culture. Barauni Refinery has
startedTPM implementation in October2002 and Coker-A unit has been
selected for implementation ofPilot model by April2004. TPM was
formally Kicked off on 30th Aug2004 after successfulimplementation
of Pilot Model at process unit. Refinery wide implementation of TPM
is plannedto be completed by 2007 end.Right from the beginning
Barauni Refinery has an exclusive Energy Conservation Cell
formonitoring energy consumption and implementation of ENCON
measures.Energy Conservation Team Structure UNIT HEAD EXECUTIVE
DIRECTORGENERALMANAGER (Tech)DY. GENERALMANAGER (TS) TA & ENCON
CELLReview existing energy level and Hydrocarbon loss.Set Plant /
Area wise targets and monitor the actualperformance.Benchmark
energy consumption and losses.Carrying out audits / surprise
checks.Initiate ENCON projects, schemes etc.Conducting surveys
like:Process ProductionCaptive PowerMonitoring Cell Managers Plant,
Utilities & OffsitesBarauni Refinery In harmony with nature 5.
20 (iv) Energy Conservation Achievements:The major projects
implemented during 2003-04 are as under: 1. Effective Utilisation
of HRSG-II A fuel efficient Gas Turbine system was commissioned on
11th Dec 02 and Heat Recovery Steam Generator was taken on range
and put on load with Gas Turbine on 21st Feb 03. The estimated
yearly benefit is 16649 SRFT /Yr. which is equivalent to 1753 Lakhs
/ Year.2. Installation of new Vacuum Ejector in AVU-IINew three
stage ejectors comprising of two ejectors in each stage were
commissioned in AVU-II in Apr2003. The O/H oil separated in
hot-well goes through a coalescer for injection to
Diesel.Benefits:The installation of ejectors has reduced the steam
consumption from the earlier value anderadicated the use of 40 ata
steam for that purpose. The system has also removed the thirdwater
system for which a separate cooling tower was being operated.The
incorporation of coalescer along with this system has also reduced
the slop generationdecreasing the load on ETP and reducing the
hydrocarbon loss. The HC recovered in thecoalescer are being
directly routed to diesel pool. Estimated benefit of the
installation ofVacuum ejector is 1496 SRFT/yr which is equivalent
to Rs. 149.6 Lakhs / Year.Barauni Refinery In harmony with nature
6. 3. Commissioning of Air Coolers in AVU-IISince inception of the
unit, the overhead systems ofK-1 and K-2 were equipped with water
condensersfor condensing the overhead vapours from K-1
andK-2.During the M&I of AVU-I four air-condensers for
K-1(AC-101A/B/C/D) and four air-condensers for K-2(AC-102A/B/C/D)
were installed for condensing theoverhead vapors cooling tower was
being operateThe condensed vapors from the air condensers are
further cooled down in trim to bring downthe temperature of the
condensate to 40C.Provision of these air condensers has reduced the
cooling water consumption; maintenancecost incurred to clean the
water condensers on regular basis and has helped to increase
theefficiency of the system. Estimated benefit of the installation
of Vacuum ejector is 570SRFT/Yr. which is equivalent to Rs. 60
Lakhs / Year.4. Commissioning of APC in AVU-I / II / IIIAdvanced
Process Control (APC) has been implemented in Crude distillation
units i.e. AVU-I /II / III in Aug03 at an investment cost of Rs.
71.25 Lakhs. Process control that has features ofoverall online
process control for optimized operation based on objective
functions provided.Based on the process conditions / disturbances
it derives inferential predictive performanceand accordingly
adjusts process conditions. A more steady and optimized operation
isachieved. Estimated benefit of APC is 1900 SRFT /yr which is
equivalent to Rs. 200Lakhs/Year.Barauni Refinery In harmony with
nature 7. 20 (v) Energy Conservation Plan & Targets:To improve
the energy performance further, the following major projects are
underimplementation / active consideration :SL.PROJECTS /
MODIFICATIONS TARGETANNUAL ANNUALNO (YEAR) SAVINGSSAVINGS (SRFT)
(Rs. Lakhs)1.Installation of BMS in TPS Boilers.2005180
182.Stoppage of operation of CRU cooling 2004 390 39tower and
connecting the CW system withPCT.3.Insulation of 9 nos. of RCO /
LSHS tanks 200518001804.Recovery of reactor blow down in
Coker-20051200120A5.Heating of desalter washwater by 2005 600
60desalter brine in AVU-I/II6.Installation of TPI in ETP 2005 150
157.Heat recovery from RFO stream in Coker-20051700170A by steam
generation @ 3 MT/Hr8.Revamping of heat exchanger
network20065000500and fractionation improvement in
AVU-I&II9.Hydrogen recovery from CRU off gas 200513600 136010.
Flare management with provision of LPG
20051200120vaporizerTotal25820 2582With the implementation of above
energy conservation projects, specific energy consumption ofthe
refinery will about 112 MBTU/BBL/NRGF.Barauni Refinery In harmony
with nature 8. 20(vi) Environment Management System:Barauni
Refinery has a full-fledged Environment Protection Cell. The worth
noting is that thiscell was established 28 years back in 1975. In
Indian oil, Environment Protection has alwaysremained a thrust
area. The Environment Protection Cell having qualified
engineerscoordinates all the activities required to achieve
continuous improvement in environmentalperformance related to
Environmental Management in the Refinery. The goals and functions
ofthe cell are: Toachieve reduction of wastesand releases giving
preference first to source reduction, second to recycle / reuse and
third to treatment and thereby maintaining effluent and emission
standards within the permissiblelimit and legislative requirements.
To obtain legislative sanctions viz. emission andeffluent
dischargeconsent, NOC, Environment Clearance for new projects and
to achieve compliance with NOC and EC conditions. To establish
prevention mechanisms by application of engineering and operational
control. System development with environment friendly.
replacement/improvement within and around the Refinery. Training /
awareness programs in the areas SOME VIEWS OF ECOLOGICAL of
environment protection within and aroundPARK the Refinery. The
Refinery has a beautiful ecological park spread over an area of 75
acres. The park Barauni Refinery In harmony with nature 9.
developed with in-house expertise and resources has lush green
lawns large variety of treesand shrubs and the wonderful ECO pond
where flora & fauna and aquatic life are thriving ontreated
effluent. The surrounding tranquil environment of the ECO pond of
park attractshundreds of migratory birds every winter. It is a
testimony of refineries dedication to fosteringenvironmental
excellence and enhancing quality of life in the region.Barauni
Refinery had developed Environmental Management System conforming
to theInternational Standards, ISO-14001 and Integrated the same
with International QualityManagement Standard, ISO-9001:2000 and
with the Occupational Health Management Systemconforming to
OHSAS-18001:1999. Refinery thus developed an Integrated
ManagementSystem called SHEQ System. SHEQ Policy, a set of
objectives and time bond action plan areset for the continual
improvement and customer satisfaction in the area of Safety,
Health,Environment & Quality.ECOLOGICAL PARKECOLOGICAL
PARKTreated Effluent Quality: PARAMETERSMINAS LIMIT 2003-2004
(AVG.)pH6.0-8.57.55OIL & GREASE, mg/litre 105.4PHENOL, mg/litre
1.00.026BOD, mg/litre15 9.75SULPHIDES, mg/litre0.50.29TSS,
mg/litre2016.8 Barauni Refinery In harmony with nature 10. 100%
compliance of effluent quality with MINAS since 1990. Maximum
recycle of treated effluent. Nil discharge to river Ganges except
in Monsoon.Emission Control:The major air pollutant from the
Refinery is SO2. The SO2 emissions are controlled right at
thesource through use of low sulphur fuel in the furnaces and
boilers. The stack emissions aremonitored periodically for SO2,
NOx, CO and SPM and have been found to be well below thelimit
specified by the CPCB as well as BSPCB.UNITSTIPULATIONS ACTUAL (AS
PER MOE&F)SO2 EMISSIONSO2 EMISSION AVUKG/ MT of crude
processed0.25 0.151 RFCCUKG/ MT of feed2.5 0.28 TPSKG/HR (MAX.)
12894 REFINERY KG/ HR 1080 450Safety Management System:Barauni
Refinery has an elaborate Safety Management System. Refinery is
following stringentOil Industry Safety Directorate (OISD) standards
and other Rules/ Acts as applicable. PeriodicSafety Audit of the
facilities and system is carried out. Each recommendations status
isthoroughly discussed in the monthly Health & Safety Committee
Meeting chaired by the topmost official of the company. No efforts
are spared to fulfill recommendations arising duringSafety Audit,
in shortest possible time.To take care of the Safety of the
refinery and surrounding and to minimise the impact of theprobable
emergencies, viz fire, explosion, toxic gas release etc., Refinery
has prepared On-SiteDisaster Management Plan and Off- Site Disaster
Management Plan, and both are dulyapproved by competent authority.
Material Safety Data Sheet (MSDS) consisting of paramountproperties
of chemicals & their safe handling is a part of Disaster
Management Plan. To checkthe efficiency and bring improvement in
the plan, periodic On-Site & Off Site mock drills
areconducted.Barauni Refinery In harmony with nature 11. ----- End
-----Barauni Refinery In harmony with nature 12. MAIN PRODUCTSLPG
:LIQUEFIED PETROLEUM GASMS:MOTOR SPIRITNAPHTHA :NAPHTHAHSD :HIGH
SPEED DIESELSKO :SUPERIOR KEROSENE OILMTO :MINERAL TURPENTINE
OILLDO :LIGHT DIESEL OILLSHS:LOW SULPHUR HEAVY STOCKRPC :RAW
PETROLEUM COKECPC :CALCINED PETROLEUM COKEP. EXT. :PHENOL
EXTRACTSL. WAX :SLACK WAXBarauni Refinery In Harmony With Nature
13. NAME OF PROCESS UNITSAVU-I:ATMOSPHERIC & VACUUM
UNIT-IAVU-II :ATMOSPHERIC & VACUUM UNIT-IIAVUIII :ATMOSPHERIC
& VACUUM UNIT-IIIPEU:PHENOL EXTRACTION UNITSDU:SOLVENT DEWAXING
UNITCCU:COKE CALCINATION UNITNSU:NAPHTHA SPLITTER UNITCRU:CATALYTIC
REFORMER UNITRFCCU:RESID FLUID CATALYTIC CRACKING UNITDHDT :DIESEL
HYDROTREATER UNITHGU:HYDROGEN GENERATION UNITSRU:SULPHUR RECOVERY
UNITARU:AMINE REGENERATION UNITSWS:SOUR WATER STRIPPER Barauni
Refinery In Harmony With Nature 14. IndianOil Energy Policy To be a
World Class performer in energy managementBy Adopting energy
efficient and environment friendlytechnologies. Benchmarking our
performance with the best in the worldand endeavoring to be ahead.
Promoting use of renewable sources of energy. Fostering a culture
of participation and innovation amongststake holders
forcontinualimprovementin energyconservation. Propagating the
message of avoiding wastage of energy tothe community.Barauni
Refinery In Harmony With Nature 15. 1. EFFECTIVE UTILISATION OF
HRSG-IIBackground :To cater the power requirement of refinery @ 6.0
MMTPA after implementation ofBarauni Refinery Expansion Projects, a
20 MW Gas Turbine along with Heat RecoverySteam Generator of
capacity 48 MT/Hr (Pr.=40 ata , Temp.= 440oC) has been
installed.Fuel efficient Gas Turbine system was commissioned on
11th Dec 02 andHeatRecovery Steam Generator (HRSG) was taken on
range and put on load with GasTurbine on 21st Feb 03. The
stabilised operation of HRSG was started in 2003-04.Observation
Made :The steam generation through HRSG is 37 MT/Hr at a power load
of 13 MW on GasTurbine.Technical & Financial Analysis Made
:Power Load on Gas Turbine 13MWFuel (Naphtha) consumption5
MT/HrEquivalent SRFT 5.2 MT/Hr0.40MT/MwSteam Generation through
HRSG 36MT/HrEquivalent SRFT 2.6 MT/HrNet fuel consumption in Power
generation through Gas Turbine2.6 MT/Hr Barauni Refinery In Harmony
With Nature 16. 0.20MT/MwSavings SRFT by stopping one Boiler 16649
MT/Yr1753Rs. Lakh/YrImpact of implementation :Operation of one
boiler stopped.2. INSTALLATION OF NEW VACUUM EJECTOR IN
AVU-IIBackground :Steam jet ejectors were used for producing vacuum
in the vacuum column with MP (10ata) steam being used as the motive
force.The vacuum system utilised direct contact of cooling water
with vacuum columnoverhead vapour and steam coming out from column
top resulting in mixing ofcondensed oil and circulating water. This
mixture was sent to a dedicated oily watersystem (called as 3rd
cooling water system). Since the emulsion of oil and water was
verydifficult to break, this resulted in higher slop generation and
subsequently higherhydrocarbon loss.Due to the use of direct
contact type condensers a separate circulating water systemwith
cooling tower and API oil separator was required. The oil separated
from these APIseparators had to be recovered as slop oil and had to
be reprocessed in the crudedistillation unit(s). It may also be
noted that total recovery of oil was not feasible andnearly 40% -
45% of the oil resulted into loss.It is evident that the above
mentioned system was energy inefficient and prone to higherslop
generation/ hydrocarbon loss. A separate cooling water system with
hot and coldwater pumps, cooling tower fans and API oil separators
had to be separately maintainedfor vacuum producing system.To
reduce energy consumption and hydrocarbon loss the vacuum producing
system ofAVU- II was revamped with the latest vacuum producing
system consisting of thefollowing items - Shell and tube type
pre-condenser and primary inter-condenser using refinery cooling
water as cooling media. Two stage steam ejector system. Barauni
Refinery In Harmony With Nature 17. Necessary piping and
instrumentation.Observation Made :Elimination of direct contact
type ejector condensers resulting in reduction ofhydrocarbon
loss.Savings in power consumption due to elimination of dedicated
cooling water systemused for direct contact type
condensers.Technical & Financial Analysis Made :A. Reduction of
Hydrocarbon Loss: Sl. No. ParticularsQuantity (MT/ Day) 1. Vacuum
slop generation (@ 5000 MT/Day9.6Tput) 2. 30% of the vacuum slop
skimmed off and 2.88recovered in AVUs. 3. Slop carry over with 3rd
system of circulating 6.72water (1 2) 4. Slop recovery from API
Separators (55%)3.70 5. Hydrocarbon loss (3 4) 3.02Annual Savings
997 MTB. Reduction in Power Consumption: Sl. No.
ParticularsQuantity (KWH) Savings from removal of 3rd system of
circulating water 1. Reduction of 2 Nos. of hot well pumps 2 X 75
KW 2. Reduction of 2 Nos. of cold water pumps 2 X 75 KW 3.
Reduction of 3 Nos. of CT fans3 X 28 KWTotal Power Consumption 234
KWHBarauni Refinery In Harmony With Nature 18. (considering 1 hot
well pump, 1 cold water pump and 3 CT fans running) Power
consumption in revamped vacuum producing system - 1.2 Nos. of hot
well oil pumps2 X 18.5 KW 2.2 Nos. of oily water pumps2 X 5.5 KW
Total power consumption 24 KWH (considering 1 hot well oil pump and
1 oily water pump running) Net Power Consumption, (234 24) KWH 210
KWH Net Annual Power Saving 1663 MW Equivalent Annual Fuel Saving
499 MT (considering 1 MW = 0.3 MT Fuel)Total annual fuel saving and
reduction of hydrocarbon loss due to revamp of vacuumproducing
system in AVU-II (A + B) = 997+499 = 1496 MTIn monetary terms the
savings is equivalent to Rupees 149.6 lakhs/ year.Impact of
implementation :Reduction of power consumption and hydrocarbon
loss.3. COMMISSIONING OF AIR COOLERS IN AVU-IIBackground :Since
inception of the unit, the overhead systems of K-1 and K-2 were
equipped withwater condensers for condensing the overhead vapours
from K-1 and K-2.During the M&I of AVU-II four air-condensers
for K-1 (AC-101A/B/C/D) and four air-condensers for K-2
(AC-102A/B/C/D) were installed for condensing the overhead vapors.
Barauni Refinery In Harmony With Nature 19. Observation Made
:Provision of these air condensers hasreduced the cooling water
consumption,maintenance cost incurred to clean thewater condensers
on regular basis and hashelped to increase the efficiency of
thesystem. Technical & Financial Analysis Made : Estimated
benefit of the installation of Vacuum ejector is 570 SRFT/Yr which
is equivalent to Rs. 60 Lakhs / Year.4. COMMISSIONING OF APC IN
AVU-I / II / III Advanced Process Control (APC) has been
implemented in Crude distillation units i.e. AVU-I / II / III in
Aug03 at an investment cost of Rs. 71.25 Lakhs. Process control
that has features of overall online process control for optimized
operation based on objective functions provided. Based on the
process conditions / disturbances it derives inferential predictive
performance and accordingly adjusts process conditions. A more
steady and optimized operation is achieved. Estimated benefit of
APC is 1900 SRFT /yr which is equivalent to Rs. 200 Lakhs/Year.
Barauni Refinery In Harmony With Nature 20. BLOCK FLOW DIAGRAM OF
PROCESS / PRODUCTION UNITS OF BARAUNI REFINERY FUEL GASLPGCRUMS
NAPHTHAKEROSENAVU H2I/ PLANTCRUDE II / DHDTHSDIII COKERLRUA /BIFO
RPC ATU/SRUFCCULPG MERICHEMSULPHUREGASOLINE MERICHEM