公开(公告)号：EP3530718A1

公开(公告)日：2019-08-28

申请号：EP18209577.8

申请日：2018-11-30

申请人： INDIAN OIL CORPORATION Ltd.

发明人： Pradeep, Ponoly Ramachandran ,  Kottakuna, Arjun Kumar ,  Prasad, Terapalli Hari Venkata Devi ,  Das, Satyen Kumar ,  Bhattacharyya, Debasis ,  Mazumdar, Sanjiv Kumar ,  Ramakumar, Sankara Sri Venkata

IPC分类号： C10G31/08 ,  C10G51/00 ,  C10G51/06 ,  C10G55/00 ,  C10G55/08 ,  C10J3/00 ,  C10G9/00 ,  C10G9/36 ,  C10G11/18

摘要： The present invention relates to a process and system for complete conversion of crude oils by integrating delayed coking process, high severity catalytic cracking process and naphtha cracking processes along with olefin recovery section, aromatic recovery section and gasifier section to maximize the crude oil conversion to valuable products like light olefins, aromatics and chemicals.

公开(公告)号：EP2940104A1

公开(公告)日：2015-11-04

申请号：EP15159358.9

申请日：2015-03-17

申请人： INDIAN OIL CORPORATION Ltd.

发明人： Das, Satyen Kumar ,  Pradeep, Ponoly Ramachandran ,  Prasad, Terapalli Hari Venkata Devi ,  Dixit, Jagdev Kumar ,  Thapa, Gautam ,  Thakur, Ram Mohan ,  Sharma, Vinod Kumar ,  Bhattacharyya, Debasis ,  Puri, Suresh Kumar ,  Gupta, Anurag Ateet ,  Kumar, Brijesh ,  Das, Biswapriya ,  Malhotra, Ravinder Kumar

IPC分类号： C10G9/00

CPC分类号： C09K15/28 ,  C10G9/00 ,  C10G9/005 ,  C10G75/04 ,  C10G2300/1033 ,  C10G2300/107

摘要： The present invention relates to a liquid phase additive comprising an alkyl nitrate; a petroleum sulphonates; an aliphatic, aromatic, cyclohexylamines or hetroalkylated lower amines; a hindered phenol based compounds; a phosphate esters and an aliphatic alcohols for use in delayed coking process with decreased coke yield and increased yield of liquid and/or gaseous product and a process for preparing the liquid phase additive. The present invention also relates to a process for thermal cracking of petroleum residue producing petroleum coke and lighter hydrocarbon products by using liquid phase additive.

摘要翻译： 本发明涉及一种液相添加剂，其包含硝酸烷基酯的; 石油磺酸盐; 在脂族，芳族，或环己胺hetroalkylated低级胺; 受阻酚系化合物; 磷酸酯和添加剂的脂族醇为具有降低的焦炭产率延迟焦化工艺和使用液体和/或气体产物的增加的产量和用于制备液相的方法。 因此，本发明通过使用液相添加剂涉及用于石油残余物生产的石油焦炭和轻质烃产物的热裂解的方法。

公开(公告)号：EP2873713A1

公开(公告)日：2015-05-20

申请号：EP14193180.8

申请日：2014-11-14

申请人： Indian Oil Corporation Ltd.

发明人： Prasad, Terapalli Hari Venkata Devi ,  Pradeep, Ponoly Ramachandran ,  Das, Satyen Kumar ,  Dixit, Jagdev Kumar ,  Rajesh ,  Om Parkash ,  Hait, Samik Kumar ,  Dalai, Eswar Prasad ,  Thakur, Ram Mohan ,  Thapa, Gautam ,  Bhattacharyya, Debasis ,  Kumar, Brijesh ,  Das, Biswapriya ,  Rajagopal, Santanam ,  Malhorta, Ravinder Kumar

IPC分类号： C10B57/06 ,  C10G9/00 ,  B01J27/16 ,  B01J27/182 ,  C10B55/00

CPC分类号： B01J27/182 ,  B01J27/16 ,  C10B55/00 ,  C10B57/06 ,  C10G9/005

摘要： The present invention is directed to novel thermal cracking additive compositions for reduction of coke yield in Delayed Coking process and method for preparing the same. The present invention also provides that the thermal cracking additive compositions of the present invention are in micron-size and nano-size. Further, the present invention provides a process of thermal cracking of heavy petroleum residue used in petroleum refineries using Delayed Coking process to produce petroleum coke and lighter hydrocarbon products with decreased coke yield and increased yield of liquid and/or gaseous products.

摘要翻译： 本发明涉及用于降低延迟焦化方法中焦炭产率的新型热裂解添加剂组合物及其制备方法。 本发明还提供本发明的热裂解添加剂组合物为微米级和纳米尺寸。 此外，本发明提供了使用延迟焦化法生产石油焦炭和轻质烃产物的炼油厂中使用的重质石油残渣的热裂解方法，其具有降低的焦炭产率和提高液体和/或气体产物的产率。

公开(公告)号：EP0922744A1

公开(公告)日：1999-06-16

申请号：EP97309155.6

申请日：1997-11-13

申请人： INDIAN OIL CORPORATION Ltd.

发明人： Mandal, Sukumar ,  Shah, Suresh Kumar ,  Bhattacharyya, Debasis ,  Murthy, Vutukuru Lakshmi Narasimha ,  Das, Asit Kumar ,  Singh, Sanjeeve ,  Thakur, Ram Mohan ,  Sharma, Shankar ,  Dixit, Jagdev Kumar ,  Ghosh, Sobhan ,  Das, Satyen Kumar ,  Santra, Manoranjan ,  Saroya, Latoor Lal ,  Rao, Marri Rama ,  Mishra, Ganga Shankar ,  Makhija, Satish

IPC分类号： C10G11/05 ,  C10G11/18

CPC分类号： B01J29/80 ,  C10G2400/20 ,  C10G2400/28

摘要： The invention relates to a process for catalytic cracking of petroleum based feed stocks to produce high yield of LPG and light olefins with C 3 and C 4 in presence of solid acidic catalyst and high pore size acidic components in a fluidized bed reactor The reactor operates in the range of 40-120 hr -1 weight hourly space velocity, 15-25 catalyst to oil ratio and riser temperature of 520-600°C.

摘要翻译： 本发明涉及一种用于在石油基原料中催化裂解的方法，以在流化床反应器中在固体酸性催化剂和高孔径酸性组分的存在下产生具有C3和C4的高产率的LPG和轻质烯烃。反应器在该范围内操作 40-120小时-1小时空速，15-25催化油比和提升管温度为520-600℃