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公开(公告)号：US20190264716A1
公开(公告)日：2019-08-29
申请号：US16206939
申请日：2018-11-30
发明人： Pravesh KUMAR , Kamal KUMAR , Darshankumar Manubhai DAVE , Ramesh KARUMANCHI , Madhusudan SAU , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： F15D1/00
摘要： A distribution unit for distributing a multi-phase fluid mixture is disclosed. The distribution unit includes a distribution body defining a first passage, and a first distal body portion having a plurality of first slots. The distribution body includes a second distal body portion having a plurality of second slots distributed on a side wall of the second distal body portion. Each of the plurality of second slots is adapted to accommodate a baffle plate. The second distal body portion includes at least one aperture formed on a bottom wall of the second distal body portion. The plurality of first slots, the plurality of second slots, and the at least one aperture are in fluid communication with the first passage to discharge the flow of the multi-phase fluid.
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2.发明申请公开(公告)号：US20170058212A1
公开(公告)日：2017-03-02
申请号：US15239363
申请日：2016-08-17
发明人： Pravesh KUMAR , Pappu NARESH , Vinay Kumar CHAUDHARY , Darshankumar Manubhai DAVE , Kamal KUMAR , Murugan BALASUNDARAM , Karumanchi RAMESH , Ganesh Vitthalrao BUTLEY , Om Prakash NANDWANI , Madhusudan SAU , Brijesh KUMAR , Biswapriya DAS
IPC分类号： C10G67/00
摘要： This invention relates to a process for hydro cracking of heavy oils. More particularly, this invention relates to a catalytic process for converting heavy oils, such as vacuum gas oil (VGO) and VGO containing a high proportion of vacuum resid (VR) to middle distillate products.
摘要翻译： 本发明涉及重油加氢裂化方法。 更具体地说，本发明涉及一种用于将重油（例如真空瓦斯油（VGO））和含有高比例真空渣油（VR）的VGO转化成中间馏分产物的催化方法。
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公开(公告)号：US20230227738A1
公开(公告)日：2023-07-20
申请号：US18152941
申请日：2023-01-11
发明人： Ponoly Ramachandran PRADEEP , Shahil SIDDIQUI , Vineeth Venu NATH , Darshankumar Manubhai DAVE , Mainak SARKAR , Satyen Kumar DAS , Madhusudan SAU , Sankara Sri Venkata RAMAKUMAR
CPC分类号： C10G67/16 , C10G31/08 , C10G67/02 , C10G9/005 , C10J3/64 , C10G69/14 , C10G2400/20 , C10G2400/30 , C10G2300/1033 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10J2300/0943 , C10J2300/164 , C10G2300/4025 , C10G2300/4081
摘要： The present invention relates to a process and system for complete conversion of crude oils by integrating Desalter unit, Atmospheric and vacuum column, high severity FCC process, Naphtha cracking process, residue slurry hydrocracking process, Delayed coking process, Selective mild hydrocracking aromatic production unit, Dehydrogenation units, Aromatic/olefin recovery section, gasifier unit along with syngas to olefins conversion section.
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公开(公告)号：US20190276752A1
公开(公告)日：2019-09-12
申请号：US16294771
申请日：2019-03-06
发明人： Mainak SARKAR , Darshankumar Manubhai DAVE , Ganesh Vitthalrao BUTLEY , Ramesh KARUMANCHI , Arun ARANGARASU , Sarvesh KUMAR , Madhusudan SAU , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： C10G67/02
摘要： The present invention relates to an assorted co-staging and counter stage hydro-treating process configuration scheme is disclosed for deep desulfurization and deep hydro-treating of diesel range hydrocarbons for obtaining diesel product having product sulfur less than 10 ppm and cetane number more than 51.
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公开(公告)号：US20190100705A1
公开(公告)日：2019-04-04
申请号：US16118332
申请日：2018-08-30
发明人： Mainak SARKAR , Darshankumar Manubhai DAVE , Ramesh KARUMANCHI , Madhusudan SAU , Ganesh Vitthalrao BUTLEY , Nepal VISHWAKARMA , Kamal KUMAR , Pravesh KUMAR , Sarvesh KUMAR , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： C10G47/24
摘要： The present invention relates to a hydrocracking reactor system and a process utilizing the same for upgrading heavy hydrocarbonaceous material to value-added products. Accordingly, an aspect of the present invention includes dispersing a liquid feedstock pre-mixed with a catalyst from top of a reactor vessel to obtain dispersed droplets having a predetermined droplet size less than 500 μm, introducing a gaseous feed comprising primarily of hydrogen from bottom of the reactor vessel to form a continuous gaseous phase throughout a cross-section of the reactor vessel, and allowing the dispersed droplets to contact the continuous gaseous phase throughout the cross-section of the reactor vessel to form reaction effluent comprising one or more lighter product hydrocarbons. The method may further include removing at least a top portion and at least a bottom portion of the reaction effluent from the reactor vessel.
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