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1. 发明授权

EP2949636B1 PROCESS FOR SIMULTANEOUS PRODUCTION OF ALCOHOLS AND OLIGOMER PRODUCT FROM HYDROCARBON FEED STOCK 有权转让
标题翻译：从碳氢化合物原料中同时生产醇和低聚物产品的方法
公开(公告)号：EP2949636B1
公开(公告)日：2018-05-09
申请号：EP15169810.7
申请日：2015-05-29
申请人： Indian Oil Corporation Limited
发明人： Saravanan, Subramani , Manna, Reshmi , Varshney, Pushkar , Chopra, Anju , Bhattacharyya, Debasis , Kumar, Brijesh , Das, Biswapriya , Malhotra, Ravinder Kumar
IPC分类号： C07C2/28 , C07C29/04 , C10G50/00 , C07C11/02 , C07C31/10 , C07C31/12 , C10L1/02 , C10L1/06
CPC分类号： C07C2/08 , B01J35/065 , B01J35/1009 , B01J35/1014 , B01J35/1061 , C07C2/28 , C07C29/04 , C07C2531/08 , C10G50/00 , C10G2400/02 , C10L1/02 , C10L1/06 , C10L1/16 , C10L1/1608 , C10L10/10 , C10L2200/0423 , C10L2270/023 , C07C11/02 , C07C31/10 , C07C31/12 , C07C31/125
摘要： The present invention relates to a process for production of oligomer products from olefinic C4 feed stocks comprising isobutene, butenes, butanes, butadienes and mixture thereof. Particularly, the present invention relates to a process for the preparation of oligomers using olefinic C4 feed stock in presence of tertiary butyl alcohol (TBA) and iso propyl alcohol (IPA).

2. 发明公开

EP3502212A1 TWO STAGE THERMAL CRACKING PROCESS WITH MULTISTAGE SEPARATION SYSTEM 有权转让
公开(公告)号：EP3502212A1
公开(公告)日：2019-06-26
申请号：EP18203869.5
申请日：2018-10-31
申请人： Indian Oil Corporation Limited
发明人： Das, Satyen Kumar , Prasad, Terapalli Hari Venkata Devi , Pradeep, Ponoly Ramachandran , Kottakuna, Arjun Kumar , Bhattacharyya, Debasis , Mazumdar, Sanjiv Kumar , Ramakumar, Sankara Sri Venkata
IPC分类号： C10G9/00 , C10G11/18 , C10G45/00 , C10G47/00 , C10G69/06
摘要： The present invention relates to Delayed Coking of heavy petroleum residue producing petroleum coke and lighter hydrocarbon products. The invented process utilizes a pre-cracking reactor for mild thermal cracking of the feedstock and intermediate multistage separation system before being subjected to higher severity thermal cracking in delayed coking process, resulting in reduction in overall coke yield.

3. 发明公开

EP3101093A1 FCC FEED INJECTOR WITH IMPROVED ATOMIZATION 有权
标题翻译： FCC-EINSPEISUNGSSPRITZDÜSEMIT VERBESSERTER ATOMISIERUNG
公开(公告)号：EP3101093A1
公开(公告)日：2016-12-07
申请号：EP16172020.6
申请日：2016-05-30
申请人： Indian Oil Corporation Limited
发明人： De, Bidyut , Khan, Shoeb Hussain , Kumaran, Satheesh Vetterkunnel , Bhattacharyya, Debasis , Kumar, Brijesh
IPC分类号： C10G11/18 , B01F5/04 , B05B7/00 , B01J4/00 , F23C10/22
CPC分类号： C10G11/18 , B01F5/0451 , B01F5/0463 , B01F5/0652 , B01F2005/0622 , B01J4/002 , B01J4/005 , B01J2208/00902 , B01J2208/0092 , B01J2208/00929 , B05B7/00 , F23C10/22 , F23G2900/50202
摘要： The present invention discloses a method and an apparatus for mixing and atomizing a hydrocarbon stream using a diluent/dispersion stream. In one embodiment, the apparatus comprises: an inner conduit and an outer conduit concentric to each other to define an annular space, said outer conduit having an inlet for receiving the hydrocarbon stream and an outlet for dispensing a mixture comprising the hydrocarbon and the dispersion/diluent streams; a diluent/dispersion steam distributor being in connection with the inner conduit and defining a central orifice and a first set of orifices, said first set of orifices adapted to direct a first portion of the dispersion/diluent stream into the annular space and said central orifice adapted to direct a second portion of the diluent/dispersion stream into the inner conduit; atleast one contraction member and expansion member, said contraction member located downstream of the first set of orifices and said expansion member located downstream said expansion member; the inner conduit located downstream of said expansion member comprises a second set of orifices, said second set of orifices disposed on a periphery of the inner conduit and adapted to dispense a second portion of the dispersion/diluent stream into the annular space.
摘要翻译：本发明公开了一种使用稀释剂/分散体流混合和雾化烃流的方法和装置。在一个实施例中，该装置包括：内部管道和彼此同心的外部管道以限定环形空间，所述外部管道具有用于接收烃流的入口和用于分配包含烃和分散体/ 稀释剂流; 稀释剂/分散体蒸汽分配器，其与所述内部管道连接并且限定中心孔口和第一组孔口，所述第一组孔口适于将所述分散体/稀释剂流的第一部分引导到所述环形空间中，并且所述中心孔口适于将所述稀释剂/分散体流的第二部分引导到所述内部导管中; 至少一个收缩构件和膨胀构件，所述收缩构件位于第一组孔口的下游，并且所述膨胀构件位于所述膨胀构件下游; 位于所述膨胀构件下游的内部管道包括第二组孔口，所述第二组孔口设置在内部管道的周边上，并且适于将第二部分分散体/稀释剂流分配到环形空间中。

4. 发明公开

EP2949636A1 PROCESS FOR SIMULATANEOUS PRODUCTION OF ALCOHOLS AND OLIGOMER PRODUCT FROM HYDROCARBON FEED STOCK 有权转让
标题翻译：程序将醇同时生产和一个寡聚物作为烃原料的
公开(公告)号：EP2949636A1
公开(公告)日：2015-12-02
申请号：EP15169810.7
申请日：2015-05-29
申请人： Indian Oil Corporation Limited
发明人： Saravanan, Subramani , Manna, Reshmi , Varshney, Pushkar , Chopra, Anju , Bhattacharyya, Debasis , Kumar, Brijesh , Das, Biswapriya , Malhotra, Ravinder Kumar
IPC分类号： C07C2/28 , C07C29/04 , C10G50/00 , C07C11/02 , C07C31/10 , C07C31/12
CPC分类号： C07C2/08 , B01J35/065 , B01J35/1009 , B01J35/1014 , B01J35/1061 , C07C2/28 , C07C29/04 , C07C2531/08 , C10G50/00 , C10G2400/02 , C10L1/02 , C10L1/06 , C10L1/16 , C10L1/1608 , C10L10/10 , C10L2200/0423 , C10L2270/023 , C07C11/02 , C07C31/10 , C07C31/12 , C07C31/125
摘要： The present invention relates to a process for production of oligomer products from olefinic C4 feed stocks comprising isobutene, butenes, butanes, butadienes and mixture thereof. Particularly, the present invention relates to a process for the preparation of oligomers using olefinic C4 feed stock in presence of tertiary butyl alcohol (TBA) and iso propyl alcohol (IPA).
摘要翻译：本发明涉及一种用于生产从C4烯烃原料包含异丁烯，丁烯，丁烷，丁二烯和它们的混合物的低聚产物的方法。具体地，本发明涉及一种使用在叔丁醇（TBA）和异丙醇（IPA）的存在C4烯烃原料低聚物的制备。

5. 发明授权

EP3101093B1 FCC FEED INJECTOR WITH IMPROVED ATOMIZATION 有权
公开(公告)号：EP3101093B1
公开(公告)日：2019-03-20
申请号：EP16172020.6
申请日：2016-05-30
申请人： Indian Oil Corporation Limited
发明人： De, Bidyut , Khan, Shoeb Hussain , Kumaran, Satheesh Vetterkunnel , Bhattacharyya, Debasis , Kumar, Brijesh
IPC分类号： C10G11/18 , B01F5/04 , B05B7/00 , B01J4/00 , F23C10/22 , B01F5/06

6. 发明公开

EP3165588A1 PROCESS FOR PRODUCTION OF SYNGAS THROUGH REGENERATION OF COKED CRACKING AGENT 有权
标题翻译：通过再生焦化裂解剂生产合成气的方法
公开(公告)号：EP3165588A1
公开(公告)日：2017-05-10
申请号：EP16184984.9
申请日：2016-08-19
申请人： Indian Oil Corporation Limited
发明人： Mukthiyar, Sadhullah , Bhanuprasad, Sayapaneni Gopinath , Saidulu, Gadari , Dalai, Eswar Prasad , Singh, Sanjeev , Kumaran, Satheesh Vetterkunnel , Kumar, Brijesh , Das, Biswapriya , Bhattacharyya, Debasis
IPC分类号： C10G47/00 , C10G47/20 , C10G11/18 , C10J3/00 , C01B3/28 , C01B3/30 , C01B3/34 , C01B3/38 , C01B3/48
CPC分类号： C01B3/12 , B01J7/02 , B01J8/0015 , B01J8/085 , B01J8/087 , B01J19/245 , B01J2208/00769 , B01J2219/24 , C01B3/02 , C01B3/28 , C01B3/30 , C01B3/34 , C01B3/38 , C01B3/48 , C01B3/56 , C01B2203/0283 , C01B2203/042 , C01B2203/045 , C01B2203/0485 , C01B2203/0883 , C10G11/00 , C10G11/182 , C10G2300/70 , C10J3/00 , Y02P20/131
摘要： The present invention relates to a process for the production of high quality synthesis gas rich in hydrogen during the process of upgrading the residual hydrocarbon oil feedstock by rejuvenating the spent upgrading material in Reformer in absence of air/oxygen without supplying external heat source other than the heat generated inside the process during combustion of residual coke deposited on the upgrading material. The present invention further relates to the apparatus used for preparation of syngas wherein said syngas thus produced is used for production of hydrogen gas. Furthermore, the present invention also provides system and method for preparing pure hydrogen from syngas.
摘要翻译：本发明涉及一种在升级残余烃油原料的过程中生产富含氢气的高品质合成气的方法，该方法是通过在没有空气/氧的情况下在重整器中重新使用废弃的升级材料而不供应除外的热源在燃烧沉积在改质材料上的残余焦炭期间在工艺内部产生的热量。本发明进一步涉及用于制备合成气的设备，其中如此生产的所述合成气用于生产氢气。此外，本发明还提供了由合成气制备纯氢的系统和方法。

7. 发明授权

EP0922744B1 Process for the production of high yield of LPG and light olefins 失效
标题翻译：一种用于生产LPG和轻烯烃的产量高处理
公开(公告)号：EP0922744B1
公开(公告)日：2003-07-02
申请号：EP97309155.6
申请日：1997-11-13
申请人： Indian Oil Corporation Limited
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

8. 发明公开

EP1609840A1 Process for conversion of hydrocarbons to saturated lpg and high octane gasoline 审中-公开
标题翻译：在西班牙语中的Verbahren zur Umwandlung von Kohlenwasserstoffen在gesättigteLPG und在Benzin mit hoher Oktanzahl
公开(公告)号：EP1609840A1
公开(公告)日：2005-12-28
申请号：EP04254364.5
申请日：2004-07-21
申请人： Indian Oil Corporation Limited
发明人： Das, Asit Kumar , Bhattacharyya, Debasis , Saidulu, Gardari , Gupta, Bandaru Venkata Hari , Ramanarayanan, Ramakrishnan , Saroya, Latoor Lal , Lakshminarayana, Konduri , Rao, Marri Rama , Upadhyay, Vinod Ramchandra , Mandal, Sukumar , Meghavathu, Deepa , Karthikeyani, Arumugam Velayutham , Kalsi, Wadhawa Ram , Singh, Arvind Pratap , Bansal, Veena , Tiwari, Ashok Kumra , Krishnan, Venkatachalam , Makhija, Satish , Ghosh, Sobhan , Raje, Niranjan Raghunath
IPC分类号： C10G11/05
CPC分类号： C10G11/182 , B01J29/084 , B01J29/40 , B01J29/80 , B01J35/0006 , C10G11/05 , C10G11/18 , C10G69/04
摘要： The present invention relates to a process for the conversion of hydrocarbon streams with 95% true boiling point less than 400°C to very high yield of liquefied petroleum gas in the range of 45-65 wt% of feed and high octane gasoline, the said process comprises catalytic cracking of the hydrocarbons using a solid fluidizable catalyst comprising a medium pore crystalline alumino-silicates with or without Y-zeolite, non crystalline acidic materials or combinations thereof in a fluidized dense bed reactor operating at a temperature range of 400 to 550°C, pressure range of 2 to 20 kg/cm 2 (g) and weight hourly space velocity in range of 0.1 to 20 hour -1 , wherein the said dense bed reactor is in flow communication to a catalyst stripper and a regenerator for continuous regeneration of the coked catalyst in presence of air and or oxygen containing gases, the catalyst being continuously circulated between the reactor-regenerator system.
摘要翻译：本发明涉及将95％真实沸点低于400℃的烃流转化成非常高产率的进料和高辛烷值汽油的45-65重量％的液化石油气的方法，所述方法包括使用含有或不含Y-沸石，非结晶酸性物质或其组合的中等孔结晶铝硅酸盐的固体可流化催化剂在烃流化床催化裂化的流化密床反应器中在400-550℃的温度范围内操作 C，2至20kg / cm 2（g）的压力范围和0.1至20小时-1的范围内的重时空速，其中所述致密床反应器与催化剂汽提器流动连通，再生器，用于在存在空气和/或含氧气体的情况下连续再生所述焦化催化剂，所述催化剂在所述反应器 - 再生器系统之间连续循环。

9. 发明授权

EP0908506B1 A fluidized catalytic cracking process and apparatus 失效
标题翻译：用于催化裂化fluitizierten方法和装置
公开(公告)号：EP0908506B1
公开(公告)日：2004-07-21
申请号：EP97307892.6
申请日：1997-10-06
申请人： Indian Oil Corporation Limited
发明人： Kumar Das, Asit , Murthy, Vutukuru Lakshmi Narasimha , Bhattacharyya, Debasis , Singh, Sanjeev , Ghosh, Sobhan , Mandal, Sukumar , Rao, Marri Rama
IPC分类号： C10G11/18 , B01J8/26
CPC分类号： C10G11/18 , B01J8/26

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