Indian Oil Corporation Limited

Jayaraj Christopher

Brijesh Kumar

Mohan Prabhu Kuvettu

Biswanath Sarkar

Arumugam Velayutham Karthikeyani

Biswapriya Das

Alex Cheru Pulikottil

Mahesh Kadgaonkar

Ravinder Kumar Malhotra

Anurag Ateet Gupta

Balaiah Swamy

Velusamy Chidambaram

Shiba Prasad Choudhury

Manoj N Kumar

Debasis Bhattacharyya

Satyen Kumar Das

Santanam Rajagopal

Ram Mohan Thakur

Satish Makhija

Naduhatty Selai Raman

Jagdev Kumar Dixit

Gopal Ravichandran

Sanjay Kumar Ray

Mahendra Pratap Singh

Pankaj Kumar Kasliwal

Venkatachalam Krishnan

Manoj Kumar

Kumaresan Loganathan

Narayanam Seshubabu

Palvannan Mohanasundaram

Mani Karthikeyan

Kapil Arya

Prasad Dalai Eswar

Mandal Maulik Mou

Sankara Sri Ramakumar

Ravinder Kumar Malhorta

The present invention relates to a catalyst product for cracking of heavy hydrocarbon feed stocks predominantly in to light olefins and processes for preparing the catalyst. More specifically the present invention relates to a process of preparing Fluidic Catalytic Cracking (FCC) catalyst additive composition. The FCC catalyst additive composition of the present invention is a LPG selective catalyst particles comprising a medium pore zeolite bonded with clay-phosphate-silica-alumina binder. The catalyst of the present invention exhibits improved selectivity towards high value components like propylene and gasoline and suppressing low value components like dry gas and bottoms.

Process and composition for preparation of cracking catalyst suitable for enhancing LPG

The present invention relates to a fluid catalytic cracking additive composition for cracking of heavy hydrocarbon feed stocks and process for preparing the additive. The additive is suitable for enhancing yields of light olefins such as propylene, isobutylene, LPG and reduces the bottom yields. The invention specifically relates to a fluid catalytic cracking additive composition comprising a pentasil zeolite, zeolites having pore size in a range of 5.4-7.7 &#x212b;, alumina, colloidal silica, kaolin clay, and phosphate, wherein the zeolites having pore size in the range of 5.4-7.7 &#x212b; is present in an amount of 1 to 10 wt % with respect to the total amount of the pentasil zeolite and zeolite having the pore size in the range of 5.4-7.7 &#x212b;.

Composition and process for preparation of cracking catalyst suitable for enhancing yields of light olefins

The invention relates to a CO oxidation promoter additive and a method of its preparation. The CO oxidation promoter additive is having improved apparent bulk density and attrition properties for use in hydrocarbon conversion during fluid catalytic cracking. The CO oxidation promoter additive has a better CO to COconversion.

CO oxidation promoter and a process for the preparation thereof

The present invention relates to a composition of attrition resistant attrition resistant catalyst particularly for FCC catalyst additives such as ZSM-5, bottom cracking additive/residue upgradation additive and GSR additive comprising aluminum phosphate binder wherein said binder comprising of 1.5 to 2.9 moles equivalent of monobasic acid for each mole of mono-aluminum phosphate (MAP). Further, the aluminum phosphate binder is added to the catalyst additive to ensure effective binding of catalyst as well as preserving catalyst activity with high selectivity towards light olefins including LPG.

Composition and a process for preparation of attrition resistant cracking catalyst suitable for enhancing light olefins

The present invention relates to a process of conversion of waste streams of petroleum refinery into industrially useful products.

Bio-conversion of refinery waste streams

The present invention is directed to a process for the simultaneous production of carbon nanotubes and product gas comprising hydrogen and lighter hydrocarbons, from a liquid hydrocarbon comprising feeding a liquid hydrocarbon in a reactor; and converting the liquid hydrocarbon with a catalyst for simultaneous production of the carbon nanotubes, hydrogen and lighter hydrocarbons, wherein the liquid hydrocarbon comprises petroleum crude oil, its products, or mixtures thereof.

Process for simultaneous production of carbon nanotube and a product gas from crude oil and its products

The present disclosure provides a ready-to-use seed composition water, a source of silica, a source of alumina, and Na0, wherein the molar ratio of H20:Na20 ranges from 5 to 20, Na20:SiO2 ranges from 0.4 to 5 and SiO2:Al203 ranges from 1.3 to 5 used in the preparation of a synthetic faujasite zeolite which has high thermal stability and higher crystallite size. It further provides a process for preparing the ready-to-use seed composition for preparation of synthetic faujasite zeolite that requires lower crystallization time. The present disclosure provides a seed composition that does not require maturing time and a reaction gel composition that has low water and soda content. The present disclosure further provides a process for the preparation of synthetic faujasite zeolite by blending seed and reaction gel reaction composition to form a seed gel composition and subjecting it to crystallization.

Ready-to-use seed composition and process thereof

Growing community of inventors

Faridabad, India

Jayaraj Christopher