Reliance Industries Limited

Indian Oil Corporation Limited

Other

Asit Kumar Das

Sukumar Mandal

Debasis Bhattacharyya

Sobhan Ghosh

Manoj Dalsingar Yadav

Satish Makhija

Gopal Ravichandran

Praveen Kumar Chinthala

Marri Rama Rao

Sateesh Daggupati

Sanjeev Singh

Swapan Kumar Ghosh

Rajeshwer Dongara

Sachchit Kumar Majhi

Satyen Kumar Das

Latoor Lal Saroya

Vinay Amte

Ajay Gupta

Biswajit Shown

Surajit Sengupta

Jagdev Kumar Dixit

Manoranjan Santra

Suyog Subhash Salgarkar

Satyanarayana Reddy Akuri

Ajit Vishwanath Sapre

Ashwani Yadav

Mahesh Gopalrao Marve

Harender Bisht

Amit Gohel

Arumugam Velayutham Karthikeyani

Ramesh Bhujade

Gadari Saidulu

Niranjan Raghunath Raje

Venkatachalam Krishnan

Ganga Shanker Mishra

Veena Rani Bansal

Arvind Pratap Singh

Chirag Dalpatbhai Panseriya

Srikanta Dinda

Sampath Nerivetla

Shubhangi Jaguste

Kalyan Chandra Nath

Tejas Dineshbhai Doshi

Amitkumar Parekh

Alok Pal

Vutukuru Lakshmi Murthy

Ankit Vipinkumar Patel

Shankar Sharma

Amit Kumar Parekh

Anil Wadhwa

Ashish Ranjan Jha

Chandra Saravanan

Vishwanath Sapre Ajit

Pinakiranjan Sankarprasad Patra

Sudhirkumar Raojibhai Patel

Anand Raj Rajan

Ashok Swamisharan Pathak

Saumya Srivastava

Arun Kumar

Gurpreet Singh Kapur

Akhilesh Kumar Bhatnagar

Ram Mohan Thakur

Satheesh Vetterkunnel Kumaran

Sanjay Kumar Ray

Pankaj Kumar Kasliwal

Veera Venkata Satya Bhaskara Sita Rama Murthy Katravulapalli

Mitra Bhanu Patel

Ashok Kumar Tiwari

Nagarathinam Shenbaga Murthy

Bandaru Venkata Hari Prasad Gupta

Pramod Kumar Bajpai

Clifton Gregg Keeler

Mukunda Madhav Baishya

Mitul Amrutbhai Ladani

Bidhayak Das

Anirban Ray

Udayan Sivathanu Ramalakshmi

Atul Kathiria

Bharat Kumar Vaja

Govind Tulsi

Jeyavel Sinha

Shubhangi Jagutse

Bibeka Hazarika

Nilamkumar Limbasiya

D P S Rana

Vinodh Rayan

Manthan A Malvanker

Paras N Shah

Mukunda Madhab Baishya

Rohit R Irabatti

Akhilesh Bhatnagar

Akuiri Satyanarayana Reddy

Rajeshwar Dongara

Yogesh Gupta

Minaz Makhania

Gobind Tulsi

Shailendra Arora

Haripada Bhunia

Pramod Kumar

Swapnil Prakash Sulakhe

The present disclosure relates to an FCC catalyst composition and a process for preparing the same. In a first aspect, there is provided an FCC catalyst composition comprising 25 to 45 wt % Y-type zeolite, 20 to 40 wt % silicon oxide, 5 to 25 wt % alumina, 5 to 35 wt % of at least one clay and 0.5 to 3 wt % of at least one rare earth oxide. The weight % of each of the component is with respect to the total weight of the composition. The FCC catalyst composition has an average particle size in the range of 45-120μ. In a second aspect, there is provided a process for preparing the FCC catalyst composition, which uses ball milled pseudoboehmite having an average particle size in the range of 1 to 8 micron and the whole process is carried out at a pH value in the range of 6 to 7.

FCC catalyst composition and a process for its preparation

A process for obtaining vanadium component in the form of vanadium oxide from gasifier slag is disclosed. The process comprises pulverizing the slag to obtain pulverized slag, which is blended with water and an alkali salt to obtain a slurry. The slurry is dried and then roasted in the presence of air to obtain a roasted slag. The roasted slag is leached to obtain a first filtrate comprising the vanadium component. The first filtrate is reacted with a magnesium salt to remove a silica component in the form of a precipitate. The silica free second filtrate is reacted with an ammonium salt to obtain ammonium metavanadate, which is further calcined to obtain the significant amount of vanadium pentoxide (VO).

Process for obtaining vanadium oxide from a gasifier slag field

The present disclosure relates to a process for recovering vanadium in the form of iron vanadate from a gasifier slag. The process comprises pulverizing the slag to obtain pulverized slag (). The pulverized slag () is soaked in water () and an alkali salt () to obtain a slurry (), followed by roasting the slurry in the presence of air to obtain roasted slag () which is leached () to obtain a first solution (). The first solution () is heated at a temperature in the range of 60° C. to 80° C. while adding an iron salt () in an amount in the range of 10 wt % to 60 wt % at a pH in the range of 4 to 10, to obtain a second solid residue () which is dried to obtain iron vanadate ().

Process for recovering vanadium in the form of iron vanadate from a gasifier slag

The present disclosure relates to a process and a system for producing synthesis gas. The carbonaceous feedstock is gasified, in the presence of at least one of oxygen and steam, in a first reactor to obtain a gaseous mixture comprising H2, CO, CH4, CO2, H2O, tar and char. The gaseous mixture is treated in a second reactor, in the presence of a catalyst, to obtain synthesis gas. The system comprises a first reactor, a connecting conduit, a second reactor, at least one cyclone separator, at least one heat exchanger and at least one synthesis gas filter unit. The process and the system of the present disclosure are capable of producing synthesis gas with comparatively higher conversion of the unreacted char.

Process and a system for producing synthesis gas

The present disclosure relates to a hydrothermally stable catalyst composition. The hydrothermally stable supported catalyst composition comprises KCOimpregnated on an amorphous silica-alumina support. The weight ratio of silica to alumina in the support is in the range of 0.1 to 1.5. The amount of KCOis in the range of 5 wt % to 60 wt % with respect to the total catalyst composition. The catalyst composition is characterized by a pore volume in the range of 0.1 cc/g to 0.9 cc/g, a surface area in the range of 40 m/g to 250 m/g and an attrition index in the range of 2% to 8%. The present disclosure also relates to a process for preparing the catalyst composition. The catalyst composition provides improved hydrothermal stability, attrition resistance, high pore volume and surface area for gasifying carbonaceous feed at low temperature, as compared to a conventional catalyst composition.

Hydrothermally stable catalyst composition and a process for preparation thereof

The present disclosure provides a method for catalytic conversion of waste plastic into liquid fuel. The method comprises thermally decomposing the waste plastic at a temperature in the range of 350 to 650&#xb0; C. and under a pressure in the range of 0.0010 psi to 0.030 psi, to obtain a gaseous stream. The gaseous stream is further subjected to four stage sequential cooling to a temperature in the range of &#x2212;5 to &#x2212;15&#xb0; C. to obtain a gas-liquid mixture comprising a gaseous fraction and a liquid fraction. The gas-liquid mixture is fed to the gas-liquid separator to obtain the gaseous fraction comprising C1 to C4 hydrocarbons and the liquid fraction comprising liquid fuel. The method of the present disclosure is simple, economical and energy efficient, which provides a high value liquid fuel with enhanced yield.

Method for catalytic conversion of waste plastic into liquid fuel

The present disclosure relates to a process for reducing the amount of carbon disulphide (CS) in a hydrocarbon feed containing C-Cfractions. The hydrocarbon feed is treated with an amine functionalized anion exchange resin (basic anion exchange resin) to obtain a mixture comprising a liquid fraction containing treated hydrocarbon and a solid mass containing an adduct of CSand the amine functionalized anion exchange resin. The so obtained liquid fraction containing the treated hydrocarbon is separated from the solid mass to obtain the hydrocarbon having CScontent less than 2 ppm. The amine functionalized anion exchange resin can be regenerated from the solid mass.

Process for reducing the amount of carbon disulphide (CS) in a hydrocarbon feed

The present disclosure relates to an FCC catalyst additive for cracking of petroleum feedstock and a process for its preparation. The FCC catalyst additive of the present disclosure comprises at least one zeolite, at least one clay, at least one binder, phosphorous in the form of PO, and at least one Group IVB metal compound. The FCC catalyst additive of the present disclosure is hydrothermally stable and has improved matrix surface area even after various hydrothermal treatments. The FCC catalyst additive of the present disclosure can be used in combination with the conventional FCC catalyst for catalytic cracking to selectively enhance the propylene and LPG yields.

FCC catalyst additive and a process for preparation thereof

The present disclosure relates to a process for capturing carbon-dioxide from a gas stream. In order to capture the carbon-dioxide, a support is provided and potassium carbonate (KCO) is impregnated thereon to form an adsorbent comprising potassium carbonate (KCO) impregnated support. The adsorbent is activated to form an activated adsorbent. The gas stream is passed through the adsorber to enable adsorption of the carbon-dioxide on the activated adsorbent to form a carbon-dioxide laden adsorbent. The carbon-dioxide laden adsorbent is transferred to a desorber for at least partially desorbing the carbon-dioxide from the carbon-dioxide laden adsorbent by passing a carbon-dioxide deficient stream through the desorber. The partially regenerated adsorbent is returned to the adsorber for adsorbing the carbon-dioxide from the carbon-dioxide. The process of the present disclosure reduces the overall energy demand by partially regenerating the adsorbent.

Process for capturing carbon-dioxide from a gas stream

The present invention provides a process for recovery of propylene and LPG from the fuel gas produced in FCC unit by contacting a heavier hydrocarbon feed with FCC catalyst. The process provides an energy efficient configuration for revamping an existing unit constrained on wet gas compressor capacity or for designing a new gas concentration unit to recover propylene and LPG recovery beyond 97 mole %. The process of the present invention provides an increase propylene and LPG recovery without loading wet gas compressor with marginal increase in liquid loads.

Process for propylene and LPG recovery in FCC fuel gas

An improved process for the catalytic gasification of a carbonaceous feedstock in a dual fluidized bed reactor for producing synthesis gas is disclosed. The disclosure uses &#x3b3;-alumina as a catalyst support i and heat carrier in the gasification zone (). The gasification zone () is operated at 700-750&#xb0; C. to prevent substantial conversion of &#x3b3;-alumina to &#x3b1;-alumina, which would manifest in the enablement of high catalyst loading and high recyclability. The catalyst is an alkali metal, preferably KCO, so that conversion proportional to total KCOto solid carbon ratio is achieved with as high KCOloading as 50 wt % on the solid support. The combustion zone () is operated at 800&#xb0;-840&#xb0; C., to prevent any conversion of the &#x3b3;-alumina to &#x3b1;-alumina, so that catalyst recyclability of up to 98% is achieved between two successive cycles.

Process for catalytic gasification of carbonaceous feedstock

The present disclosure provides a single compression system and a process for capturing carbon dioxide (CO) from a flue gas stream containing CO. The disclosure also provides a process for regeneration of the carbon dioxide capture media.

Single compression system and process for capturing carbon dioxide

The present invention relates to a stabilized inorganic oxide support for capturing carbon dioxide from gases having high regeneration capacities over many cycles. The method for preparing the stabilized inorganic oxide support includes stabilizing an alumina-containing precursor by either calcining or steaming, impregnating an alkali or alkaline earth compound into the stabilized alumina-and drying the alkali or alkaline earth compound-impregnated stabilized alumina. The stabilized inorganic oxide support can be regenerated at lower temperatures between 100 and 150&#xb0; C. The carbon dioxide adsorption capacity of the regenerated support is between 70 and 90% of the theoretical carbon dioxide adsorption capacity.

Stabilized inorganic oxide supports and adsorbents derived therefrom for carbon dioxide capture

A method for removing chloride impurities from a heavy hydrocarbon stream is disclosed. The heavy hydrocarbon stream is contacted with a stripping medium at a temperature ranging between 100-450&#xb0; C. and at a pressure ranging between 0.1-2 bar with ratio of the heavy hydrocarbon stream to the stripping medium ranging between 1-30; wherein the temperature is maintained below the initial boiling point of the hydrocarbon stream.

Method for removing chlorides from hydrocarbon stream by steam stripping

A computer implemented blend control system and method for preparation of a hydrocarbon blend from a plurality of components drawn from respective component tanks have been disclosed. The system, in accordance with the present disclosure includes at least one sensor and analyzer adapted to sense and analyze a first attribute of at least one of the components for obtaining first attribute data. The system further includes, at least one optimizer having a data storage means for storing attribute based model data. The optimizer receives the first attribute data and transmits the received first attribute data to a comparator which computes an optimized proportion data between each of the component streams to enable selective drawing of each of the component streams in accordance with the optimized proportion data for preparing the hydrocarbon blend.

System and method for preparing hydrocarbon blend from multiple component streams

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Gujarat, India

Asit Kumar Das