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1.发明授权
公开(公告)号：EP0957151B1
公开(公告)日：2003-07-16
申请号：EP98303696.3
申请日：1998-05-12
发明人： Ghosh, Sobhan , Makhija, Satish , Kuvettu, Mohan Prabhu , Krishnan, Ventachalam , Ray, Sanjay Kumar , Santra, Manoranjan , Thakur, Ram Mohan , Dixit, Jagdev Kumar
CPC分类号： C10G11/05 , B01J29/084
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2.发明公开A LIQUID PHASE ADDITIVE FOR USE IN THERMAL CRACKING PROCESS TO IMPROVE PRODUCT YIELDS 审中-公开液相添加剂FOR USE IN抗热裂一种提高产品的成品率
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
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。
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公开(公告)号：EP0742044B1
公开(公告)日：2001-10-04
申请号：EP95303151.5
申请日：1995-05-10
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4.发明公开Process for the preparation of a CO oxidation promoter 失效Verfahren zur Herstellung von CO-Oxydationspromotor
公开(公告)号：EP0742044A1
公开(公告)日：1996-11-13
申请号：EP95303151.5
申请日：1995-05-10
发明人： Kuvettu, Mohan Prabhu , Ray, Sanjay Kumar , Shende, Viswas Bhajandas , Ghosh, Sobhan , Santra, Manoranjan , Debnath, Shyamal , Sharma, Shankar , Thakur, Ram Mohan , Dixit, Jagdev Kumar
摘要： A process for the preparation of a CO oxidation promoter which comprises in preparing a slurry of colloidal silica/clay and a binder with peptised pseudoboehmite. The slurry is then subjected to the step of spray drying to obtain microspheres. The microspheres are calcined and then impregnated with platinum.
摘要翻译： 一种用于制备CO氧化促进剂的方法，其包括在制备胶体二氧化硅/粘土的浆料和具有胶溶的假勃姆石的粘合剂。 然后将浆料进行喷雾干燥的步骤以获得微球体。 将微球体煅烧，然后用铂浸渍。
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5.发明公开Thermal cracking additive compositions for reduction of coke yield in delayed coking process 审中-公开添加剂Kraken zur Redizierung der Koksausbeute在verzögertemVerkokungsverfahren
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
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。
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6.发明公开A fluidized catalytic cracking catalyst and a process for the preparation thereof 失效Fliessbettkrackkatalysator和Verfahren zu seiner Herstellung
公开(公告)号：EP0957151A1
公开(公告)日：1999-11-17
申请号：EP98303696.3
申请日：1998-05-12
发明人： Ghosh, Sobhan , Makhija, Satish , Kuvettu, Mohan Prabhu , Krishnan, Ventachalam , Ray, Sanjay Kumar , Santra, Manoranjan , Thakur, Ram Mohan , Dixit, Jagdev Kumar
CPC分类号： C10G11/05 , B01J29/084
摘要： A process for preparation of fluidized catalytic cracking (FCC) catalyst, comprising silicon stabilized large crystallite sized synthetic faujasite zeolite, aluminum depleted and normal kaolin clay, alumina and silica. The cracking catalyst is highly active and selective for bottom upgradation, it produces less coke and higher gasoline and total cycle oil. (TCO) and possesses improved metal tolerance properties when evaluated and compared with a commercial catalyst under conditions of a typical FCC unit in a petroleum refinery.
摘要翻译： 一种制备流化催化裂化（FCC）催化剂的方法，包括硅稳定的大晶粒大小的合成八面沸石沸石，贫铝和正常的高岭土，氧化铝和二氧化硅。 裂解催化剂对于底部升级具有高度活性和选择性，它产生较少的焦炭和较高的汽油和总循环油。 （TCO），并且在石油炼厂中典型的FCC装置的条件下，与商业催化剂进行比较时，具有改善的金属耐受性。
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7.发明公开Process for the production of high yield of LPG and light olefins 失效Verfahren zur Herstellung von LPG und Leichtolefinen mit hohen Ausbeuten
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
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
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℃
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