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公开(公告)号：US11194301B2
公开(公告)日：2021-12-07
申请号：US16355191
申请日：2019-03-15
申请人： UOP LLC
摘要： A process for reducing pressure of a vapor stream wherein the vapor stream rotates a turbine wheel within the turbine to transmit rotational movement to an electrical generator and generate electricity. The resulting lower pressure vapor stream reduces a partial pressure of a hydrocarbon vapor or is injected into a reactor to reduce a temperature in the reactor. A recovered electric power measuring system comprises at least one processor; at least one memory storing computer-executable instructions; and at least one receiver configured to receive data from a sensor on an electrical powerline connected to a generator of a turbine, the turbine in fluid communication with a vapor stream wherein the turbine reduces the pressure of the vapor stream and the resulting lower pressure vapor stream is injected into a reactor to reduce a temperature in the reactor or to reduce a partial pressure of hydrocarbon vapor in the reactor.
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2.发明申请FLUID CATALYTIC CRACKING PROCESS INCLUDING ADSORPTION OF HYDROGEN AND A CATALYST FOR THE PROCESS 有权流体催化裂化过程，包括加氢过程中氢和催化剂的吸附公开(公告)号：US20150166431A1
公开(公告)日：2015-06-18
申请号：US14108384
申请日：2013-12-17
申请人： UOP LLC
发明人： Matthew Lippmann , Alex A. Rio , Keith A. Couch
IPC分类号： C07C4/06
摘要： A process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) adsorbing hydrogen on the catalyst during cracking; and (c) producing a cracked product, preferably propylene, wherein the catalyst comprises (i) a matrix, (ii) a catalytically active material, and (iii) a hydrogen adsorption material. Another process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) contacting the hydrocarbon feed with a hydrogen adsorption material; (c) adsorbing hydrogen on the hydrogen adsorption material during cracking; and (d) producing a cracked product, wherein the catalyst comprises (i) a matrix and (ii) a catalytically active material.
摘要翻译： 催化裂解方法包括以下步骤：（a）在催化裂化条件下使烃进料与催化剂接触; （b）在裂化过程中在催化剂上吸附氢; 和（c）产生裂化产物，优选丙烯，其中催化剂包含（i）基体，（ii）催化活性材料和（iii）氢吸附材料。 另一种催化裂化方法包括以下步骤：（a）在催化裂化条件下使烃进料与催化剂接触; （b）使烃进料与氢吸附材料接触; （c）在开裂期间在氢吸附材料上吸附氢; 和（d）产生裂化产物，其中所述催化剂包含（i）基质和（ii）催化活性材料。
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公开(公告)号：US10851315B1
公开(公告)日：2020-12-01
申请号：US16454506
申请日：2019-06-27
申请人： UOP LLC
发明人： Mark P. Lapinski , Rajeswar Gattupalli , Bryan K. Glover , Mohamed Shakur , Keith A. Couch , Michael W. Penninger , Soumendra Mohan Banerjee , Deepak Bisht , Gautam Pandey , Amit Sharma , Priyesh Jayendrakumar Jani , Nishesh Garg
摘要： Processes for the production of a gasoline blend. A C7 portion of a naphtha stream is first isomerized to increase the branched, iso-paraffins, and then, the isomerized effluent is passed to a dehydrogenation reaction zone. In the dehydrogenation zone, the C7 saturated hydrocarbons are convert to C7 olefins. The C7 olefins have a higher octane number than the C7 saturated hydrocarbons, and the branched olefins have a higher octane number than the normal olefins. The C7 olefins can be blended in a gasoline pool. C5 and C6 hydrocarbons can be isomerized and dehydrogenated as well, separately or with the C7 components.
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4.发明授权公开(公告)号：US09701913B2
公开(公告)日：2017-07-11
申请号：US14108384
申请日：2013-12-17
申请人： UOP LLC
发明人： Matthew Lippmann , Alex A. Rio , Keith A. Couch
摘要： A process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) adsorbing hydrogen on the catalyst during cracking; and (c) producing a cracked product, preferably propylene, wherein the catalyst comprises (i) a matrix, (ii) a catalytically active material, and (iii) a hydrogen adsorption material. Another process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) contacting the hydrocarbon feed with a hydrogen adsorption material; (c) adsorbing hydrogen on the hydrogen adsorption material during cracking; and (d) producing a cracked product, wherein the catalyst comprises (i) a matrix and (ii) a catalytically active material.
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5.发明申请公开(公告)号：US20180273444A1
公开(公告)日：2018-09-27
申请号：US15994945
申请日：2018-05-31
申请人： UOP LLC
CPC分类号： C07C5/2729 , C07C5/2767 , C07C5/367 , C07C6/126 , C10G69/06 , C10G69/123 , C07C15/08
摘要： The present subject matter describes processes for increasing overall aromatics and xylenes yield in an aromatics complex. More specifically, the process for increasing overall aromatics and xylenes yield in an aromatics complex accomplishes the increased yields by incorporating an A8-A10 isomerization step into the aromatics complex. This isomerization integration increases the para-xylene.
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公开(公告)号：US20190286081A1
公开(公告)日：2019-09-19
申请号：US16355191
申请日：2019-03-15
申请人： UOP LLC
摘要： A process for reducing pressure of a vapor stream wherein the vapor stream rotates a turbine wheel within the turbine to transmit rotational movement to an electrical generator and generate electricity. The resulting lower pressure vapor stream reduces a partial pressure of a hydrocarbon vapor or is injected into a reactor to reduce a temperature in the reactor. A recovered electric power measuring system comprises at least one processor; at least one memory storing computer-executable instructions; and at least one receiver configured to receive data from a sensor on an electrical powerline connected to a generator of a turbine, the turbine in fluid communication with a vapor stream wherein the turbine reduces the pressure of the vapor stream and the resulting lower pressure vapor stream is injected into a reactor to reduce a temperature in the reactor or to reduce a partial pressure of hydrocarbon vapor in the reactor.
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公开(公告)号：US10214465B2
公开(公告)日：2019-02-26
申请号：US15994945
申请日：2018-05-31
申请人： UOP LLC
摘要： The present subject matter describes processes for increasing overall aromatics and xylenes yield in an aromatics complex. More specifically, the process for increasing overall aromatics and xylenes yield in an aromatics complex accomplishes the increased yields by incorporating an A8-A10 isomerization step into the aromatics complex. This isomerization integration increases the para-xylene.
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