RIL’s Existing Refinery At Jamnagar, Gujarat
International Conference on Refining Challenges & Way Forward 16-17 April 2012, New Delhi
Reliance Industries Limited
RAJARAMAN J.
Reliance Industries Limited Techno-Commercial Aspects in - - PowerPoint PPT Presentation
Reliance Industries Limited Techno-Commercial Aspects in Opportunity Crude Processing - A Refiners Perspective International Conference on RAJARAMAN J. Refining Challenges & Way Forward 16-17 April 2012, New Delhi RILs Existing
RIL’s Existing Refinery At Jamnagar, Gujarat
International Conference on Refining Challenges & Way Forward 16-17 April 2012, New Delhi
RAJARAMAN J.
RIL’s Existing Refinery At Jamnagar, Gujarat
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India’s largest private sector enterprise with strong financials (FY April 2010-March 2011): Revenue of $58.0 billion EBDIT of over $ 9.2 billion Industry leading position across businesses Integrated energy chain in Upstream, Refining and Petrochemicals Successfully completed transformational initiatives and created world-scale facilities Sights set on growth initiatives that are unparalleled in scope, scale and value
Revenues Gaining momentum to achieve the next phase of significant growth
Oil & Gas 5.8% Others 0.2% Refining 72.7% Petchem 21.3% Oil & Gas 26.6% Others 0.1% Refining 36.4% Petchem 36.9%
EBIT
RIL’s Existing Refinery At Jamnagar, Gujarat
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Transportation & handling Heated vessels, heated receipt/storage facilities
higher freight.
Infrastructure for long term intake. Wax precipitation Blending with compatible grades Additional cost towards procuring complimentary grades Products quality : Cold properties of diesel viz. Cold filter plugging point, Cloud point Addition of Pour Point Depressant in diesel; Limit % in blend Cost towards additives Parrafinicity may lead to higher yield of LPG/Gasoline in FCC Monitor VGO properties FCC t 'put could be limiting resulting in potential loss (if processing large % of HPP crude)
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Transportation & pumping Dilute and transport Heat and Transport Price differential gets adjusted to the extent of cost
Slower release of water in storage tanks - Tendency to form stable emulsions Segregated tanks for Heavy grades High retention time and hence, higher inventory carrying cost Blending: Stratification resulting in layering Controlled blending and tankage segregation Inventory carrying cost and possibly demurrage penalties Dehydration constraints Desalter modifications in terms of size and current capacity (amperage) Investment on desalter modification Higher VGO & Vacuum residue Choose appropriate complementary crude to blend Higher basket price due to higher cost of complementary grades Higher % processing would require investment decision
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Reduction in Hydrotreater / FCC catalyst life cycle VGO Nitrogen limit; High severity operation
nitrification of feedstock.
turnaround cycle Inferior FCC yield - increased heavy ends i.e. slurry
Corrosion in VGO hydrotreater. Nitrogen in VGO to be limited. Stepped up inspection for Hydrotreater internals Adverse affect on health of the reactor.
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Arsenic & Mercury a) Mercury (organic type) – In naphtha, poisons Petro-Chemical cracker catalyst b) Mercury (inorganic type) & Arsenic – Environmental hazard (kills biomass in ETP) Nickel & Vanadium in VGO a) Hydrotreater, Hydro Cracker, FCC catalyst poisoning; Severely impact catalyst life cycle. b) Gas make in FCC increases, disturbing the yield c) Improper cracking in Hydro-cracker–inferior yield Presence of metals in crude oil leads to improper separation of salts in the desalter. In absence of specific treatment, need to be managed thru’ blending.
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RIL’s Existing Refinery At Jamnagar, Gujarat
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