The Jamnagar Gasification Project



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Transcription:

Gasification Technologies Conference 2011 Reliance Industries Limited The Jamnagar Gasification Project by Dr. Partha Maitra Thank You Reliance Industries Ltd. India San Francisco, USA 9 12 October, 2011

Index 1. Vision 2. Reliance 3. Scope 4. Configuration 5. Project 6. Conclusion 2

Vision Boost Jamnagar refinery margins, by petcoke gasification Eliminate high cost LNG imports, w/ syngas from gasification Supply petrochem feed w/sustainable competitiveness Create platform to diversify to unconv. fuels + petrochem Gasification as alternate processing 3

Reliance RIL, $ bn 2010-11 2011-12(annualized) Sales 58.0 74.8 Exports 32.9 46.3 EBDIT 9.2 9.8 Cash profit 7.7 8.0 Net profit 4.5 5.1 Operates world s largest refinery Top 5 in deep water E&P 3 shale gas projects in the US Global #1 in polyester 22% CAGR in sales and 25% CAGR in profits since 1977 IPO Growth company 4

Jamnagar refinery Jamnagar = Largest refinery in the world = 1.34 mb/d crude feed in 2010 = 1.5% of global refining VR processing = 2 cokers = 346 kb/d combined capacity Petcoke Gasification = 6.4 mmt/yr, high S petcoke = Lowest value refinery product = Value add petcoke w/ gasification = Bottomless refinery w/ gasification = Significant boost to refinery margins = Widen margin delta over refinery peers Sustainable competitiveness in refining 5

LNG Demand driver # gasifier Comments LNG imports 4.2 Supplemental fuel Total gasifiers 4.2 Support Jamnagar refinery Gasifier size Beat LNG price = 2 mmscm/d of syngas, NG equiv = Exploit economy of scale = Min capex = Target lowest life cycle cost = Minimize capex + opex of gasification = Syngas at a price discount to LNG Low cost energy platform to eliminate LNG 6

Petrochem feed Refinery offgas(rog) = 400 kt/yr ethylene = 1200 kt/yr ethane ROG for petrochem ROG Cracker = Recover ethylene + propylene = Recover ethane = Crack ethane to ethylene = Recover hydrogen = 1350 kt/yr ethylene = 150 kt/yr propylene = World scale 5.4 gasifiers for ROG Cracker feed + fuel Competitive feed for olefins 7

CO recovery Feed = Recover CO from syngas = Feed CO for acetyl chemicals = Import methanol for feed Acetyl chemicals = Acetic acid = Acetic acid derivatives 0.4 gasifiers for Acetyl feed + fuel Competitive platform for acetyl chemicals 8

Scope Demand # Comment LNG substitution 4.2 Power & steam, H 2 ROG Cracker 5.4 SNG, power + steam Acetyl chemicals 0.4 CO recovery Total gasifiers 10 Demand driven Demand = 10 large gasifiers = 2 mmscm/d NG equiv. syngas/gasifier = 20 mmscm/d total World s largest gasification complex 9

Feed Supply # Comment Petcoke 7.5 Jamnagar cokers Petcoke/coal 2.5 Supplemental feed Total gasifiers 10.0 Feed shortfall = 25% petcoke = 2.1mmt/yr petcoke import Coal = Select low grade coal = Match syngas demand w/ 10 gasifiers = 3.5mmt/yr or 35% coal import Feed basis = 65/35 petcoke + coal blend =10 mmt/yr = 100% petcoke = 8.5 mmt/yr 75% captive feed w/petcoke 10

Product Syngas utilization # Comment Power & steam 5.7 Cogen. power plant (existing + new) H 2 1.4 Substitute existing H 2 plants SNG 2.5 RFG for process heaters CO 0.4 Acetyl chemicals Total 10.0 Design enabled for 8 mmt/yr CO 2 recovery 100% captive consumption of syngas 11

Configuration Min capex Largest gasifier w/min scale up risks 2 mmscm/d NG equiv. syngas, per gasifier 2 gasifiers + 1 ASU per standard gasifier module Repeat design of standard gasifier module Min opex HHP steam gen in syngas cooler/sng Employ pinch design Overall integration Licensor selection Low syngas cost Petcoke experience Min technology risk Min lifecycle cost for gasification 12

Project Gasification Gasification ASU OGBL OSBL 10 gasifiers 2 mscm/d syngas/gasifier 0.85 mmt/yr petcoke 1.0 mmt/yr petcoke + coal ASU = Air seperation unit OGBL = Outside gasification battery limit OSBL = Outside battery limit 5 trains O 2 to gasifier Processing 5250 t/d O 2 /ASU AGR SRU/TGT SWS CO shift Product PSA for H2 SNG CO recovery Utility CPP/power & steam Desal Water system Fuel system Offsite ETP Flare Feed system Sulphur/slag Manage project effectively 13

Schedule Reliance + PMC Licensor EPCM contractor Suppliers ASU OGBL Target 36 months for 4 gasifiers Target 42 months for 10 gasifiers Fast track schedule 14

Conclusion Ensure competitive gasification w/ lowest life cycle cost Value add low cost petcoke/coal to boost refinery margins Substitute LNG w/syngas from gasification Generate ethylene + ethane feed for petrochem Generate CO for acetyl chemicals Diversify into unconventional fuels (XTL) in future Bet on gasification 15

Thank You