Indian Oil Corporation Limited

Kamlesh Gupta

Sankara Sri Venkata Ramakumar

Debasis Bhattacharyya

Sanjiv Kumar Mazumdar

Mohan Prabhu Kuvettu

Sobhan Ghosh

Arumugam Velayutham Karthikeyani

Ram Mohan Thakur

Satish Makhija

Sanjay Kumar Ray

Hima Bindu Doosa

Mitra Bhanu Patel

Gurpreet Singh Kapur

Madhusudan Sau

Ravinder Kumar Malhotra

Sukumar Mandal

Santanam Rajagopal

Biswanath Sarkar

Gadari Saidulu

Gopal Ravichandran

Balaiah Swamy

Dheer Singh

Saravanan Subramani

Pankaj Kumar Kasliwal

Reshmi Manna

Vineeth Venu Nath

Venkatachalam Krishnan

Latoor Lal Saroya

Sadhullah Mukthiyar

Pushkar Varshney

Manoj Kumar Bhuyan

Prosenjit Maji

Venkatchalam Krishnan

Ganga Shankar Mishra

Gopal Ravi Chandran

Ganga Shankar Misra

Kumar Brijesh

The present invention relates to a process for production of high yield of hydrogen by carrying out the dry reforming of the dry gas generated from the process itself by utilizing the same catalyst for cracking and producing high yield of light olefins such as ethylene, propylene and butylenes from residue feedstocks.

Process for producing hydrogen and light olefins from resid fluid catalytic cracking

The invention discloses a novel method for preparation of highly active and selective dehydrogenation catalyst, comprising of metal oxide of group VIB elements of periodic table, and at least one metal oxide from group IA and/or group VIII, supported on alumina or silica or mixture thereof, wherein the accessibility to active sites and dispersion of metal oxides is enhanced by the addition of carbonaceous material such as coke derived from coal or petroleum coke or any other form of carbon, during catalyst preparation and its combustion thereof during calcination.

Highly active catalyst for dehydrogenation of alkanes and method of preparation thereof

The present invention is related to an integrated process for enhancing the yields of propylene and other light olefins from Fluid catalytic cracking (FCC) process in combination with Oxidative propane dehydrogenation (OPDH) where in a hydrocarbon stream from Propylene recovery section consisting of propane predominantly, is converted to high value light olefins primarily Cand Colefins by catalytic oxidative dehydrogenation using carbon dioxide from FCC flue gas exiting the regenerator. Several process configurations for the conversion of Cand Calkanes to their respective alkenes separately or simultaneously by integrating with FCC are provided.

Integrated fluid catalytic cracking and oxidative propane dehydrogenation process

The present invention relates to a process for etherification of mixed olefinic light naphtha boiling in the range of C5-90&#xb0; C. cut with simultaneous minimization of unreacted methanol concentration in the product. The etherification of mixed olefinic light naphtha produces the high octane blending component which can be blended directly in the gasoline pool without any recovery of the feed oxygenates like methanol, ethanol etc. which conventionally uses energy intensive separation processes.

Process for etherification of mixed olefinic light naphtha and simultaneous reduction of methanol in the product

The present invention provides a catalyst composition for use in a catalytic cracking process, said catalyst composition comprises 3.5 to 15.5% of pentasil zeolite, 9 to 40% of ultra-stable Y (USY) or rare earth exchanged USY (REUSY) zeolite, 3.5 to 15% of large pore active matrix based bottom up gradation component and 0.3 to 3% of a metal trap component, the percentage being based on weight of the catalyst composition. The present invention also provides a process for preparing the said catalyst composition and a catalytic cracking process comprising contacting the said catalyst composition with a feedstock.

Catalyst composition for fluid catalytic cracking, process for preparing the same and use thereof

A process for preparing bi-functional catalyst for Fluid Catalytic Cracking (FCC), that comprises molecular sieves, modified clay and semi-basic alumina and the catalyst for highly effective cracking of high boiling petroleum feedstock to provide simultaneously, enhanced yields of Liquefied Petroleum Gas (LPG) and reduction of undesirable bottoms.

Process for preparation of bi-functional fluid catalytic cracking catalyst composition

A fluid catalytic cracking additive composition to obtain enhanced yield of Liquified Petroleum Gas in catalytic cracking of high boiling petroleum feed stocks comprising 4 to 20 wt. % aluminum phosphate composite, 1-40 wt. % crystalline molecular sieve Zeolites from the group selected from mordenite ZSM-5, Beta and mixtures thereof and 40-90 wt. % clay.

Process for the preparation of fluid catalytic cracking catalyst additive composition

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Faridabad, India

Kamlesh Gupta