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1. 发明申请

US20150068953A1 ENHANCED PROCESSES TO PRODUCE VALUE-ADDED PRODUCTS FORM LIGHT GASES 有权
标题翻译：生产价格增值产品形式的轻质气体的增强方法
公开(公告)号：US20150068953A1
公开(公告)日：2015-03-12
申请号：US14463858
申请日：2014-08-20
申请人： H R D Corporation
发明人： Abbas HASSAN , Aziz HASSAN , Rayford G. ANTHONY , Gregory G. BORSINGER
IPC分类号： B01J19/24 , C10G11/18 , C01B3/26 , C07C5/333
CPC分类号： C10G49/22 , B01F7/00766 , B01F13/1016 , B01J8/222 , B01J19/1806 , B01J2208/00283 , B01J2219/0011 , B01J2219/00189 , C01B3/22 , C01B3/24 , C01B3/26 , C01B3/50 , C01B2203/0272 , C01B2203/0277 , C01B2203/10 , C01B2203/1041 , C01B2203/1235 , C01B2203/1241 , C01B2203/1247 , C01B2203/1276 , C01B2203/148 , C10G2/30 , C10G2/342 , C10G9/00 , C10G45/00 , C10G45/02 , C10G45/12 , C10G47/00 , C10G47/24 , C10G49/10 , C10G49/20 , C10G50/00
摘要： Herein disclosed is a method of producing value-added product from light gases, the method comprising: (a) providing light gases comprising at least one compound selected from the group consisting of C1-C6 compounds and combinations thereof; (b) intimately mixing the light gases with a liquid carrier in a high shear device to form a dispersion of gas in the liquid carrier, wherein the dispersion is supersaturated with the light gases and comprises gas bubbles at least some of which have a mean diameter of less than or equal to about 5 micron(s); (c) allowing the value-added product to form and utilizing vacuum to extract unreacted light gases from the liquid carrier; (d) extracting the value-added product; wherein the value-added product comprises at least one component selected from the group consisting of higher hydrocarbons, hydrogen, olefins, alcohols, aldehydes, and ketones. A system for producing value-added product from light gases is also disclosed.
摘要翻译：本文公开了一种从轻质气体生产增值产品的方法，该方法包括：（a）提供包含至少一种选自C1-C6化合物及其组合的化合物的轻质气体; （b）将轻质气体与高剪切装置中的液体载体紧密混合以形成液体载体中的气体分散体，其中该分散体与轻质气体过饱和，并且包括气泡，其中至少一些具有平均直径小于或等于约5微米; （c）允许增值产品形成和利用真空从液体载体中提取未反应的轻质气体; （d）提取增值产品; 其中所述增值产物包含至少一种选自高级烃，氢，烯烃，醇，醛和酮的组分。还公开了一种从轻质气体生产增值产品的系统。

2. 发明授权

US06485631B1 Process for thermal, and optionally catalytic, upgrading and hydrogenation of hydrocarbons 有权
标题翻译：碳氢化合物的热和任选催化，升级和氢化的方法
公开(公告)号：US06485631B1
公开(公告)日：2002-11-26
申请号：US09492658
申请日：2000-01-27
申请人： Olav Ellingsen
发明人： Olav Ellingsen
IPC分类号： C10G4500
CPC分类号： C10G49/10 , C10G47/24 , Y10S585/921 , Y10S585/922
摘要： A process for thermal and, optionally, catalytic upgrading and hydrogenation of hydrocarbons is described, wherein the hydrocarbons (oil) with a lower API grade is passed through one or more reactors connected in parallell or in series, preferably in series, in liquid state where it under pressure and intense agitation at a given temperature is thermally upgraded by increasing API, and that the product is discharged in liquid state, and whereby the agitation is effected by whipping elements, optionally made of a catalytic material acting as a catalyst in upgrading the oil in the reactor.
摘要翻译：描述了用于烃的热和任选地催化升级和氢化的方法，其中具有较低API级别的烃（油）通过一个或多个反应器，其以液体状态平行或串联连接，优选串联连接，在给定温度下的压力和强烈搅拌下，通过增加API进行热升级，并且产物以液态排出，由此搅拌是通过搅拌元件进行的，所述搅打元件任选地由用作催化剂的催化剂制成，以升级油在反应堆中。

3. 发明申请

US20160362615A1 HYDROCONVERSION PROCESS TO UPGRADE THE TRANSPORT PROPERTIES OF HEAVY AND EXTRA-HEAVY CRUDE OILS AT LOW SEVERITY CONDITIONS USING DISPERSED-PHASE CATALYST 有权
标题翻译：使用分相催化剂在低严重条件下提高重油和超重油的运输特性的降解过程
公开(公告)号：US20160362615A1
公开(公告)日：2016-12-15
申请号：US15182319
申请日：2016-06-14
申请人： INSTITUTO MEXICANO DEL PETROLEO
发明人： Jorge ANCHEYTA JUAREZ , Sergio RAMIREZ AMADOR , Zenaida Carolina LEYVA INZUNZA , Alexander QUITIAN ARCINIEGAS
IPC分类号： C10G47/04 , C10G65/14 , C10G45/08 , C10G45/00 , C10G45/04 , C10G45/06
CPC分类号： C10G47/04 , C10G45/04 , C10G45/06 , C10G45/08 , C10G45/14 , C10G47/02 , C10G47/24 , C10G49/10 , C10G65/14 , C10G2300/302 , C10G2300/308
摘要： The present invention relates to a catalytic hydroconversion process in dispersed phase of extra-heavy and heavy crude oils for upgrading their transport properties, that operates at low severity conditions, in such a way that the obtained product can be transported by conventional pumping to the distribution and refining centers.The main technical contributions of the hydroconversion process in dispersed phase of this invention to upgrade the transport properties of heavy and extra-heavy crudes are:Compact size and can be localized next to the production facilities on ground or offshore Use of operating conditions at low severity Reduction of the viscosity and increase of the API gravity at values that allow the transportation by pipeline of heavy or extra-heavy crude Upgrading of the crude oil properties in a permanent way Hydrocarbon and gases from production centers are used as supplies Operation in dispersed phase avoiding plugging problems Use of low-cost disposable catalysts at low concentrations

4. 发明申请

US20130130033A1 ADDITIVE FOR HYDROCONVERSION PROCESS AND METHOD FOR MAKING AND USING SAME 审中-公开
标题翻译：加氢方法及其制备方法和使用方法
公开(公告)号：US20130130033A1
公开(公告)日：2013-05-23
申请号：US13471567
申请日：2012-05-15
申请人： Carlos Canelon , Angel Rivas , Omayra Delgado , Miguel Paiva , Giuseppe Di Sarli , Luis Zacarias
发明人： Carlos Canelon , Angel Rivas , Omayra Delgado , Miguel Paiva , Giuseppe Di Sarli , Luis Zacarias
IPC分类号： B01J35/00
CPC分类号： B01J20/30 , B01J20/3021 , B01J20/3078 , B01J35/0026 , C10G49/10 , C10G2300/205 , C10G2300/4025 , C10G2300/80 , Y10T428/2982
摘要： An additive for hydroconversion processes includes a solid organic material having a particle size of between about 0.1 and about 2,000 μm, a bulk density of between about 500 and about 2,000 kg/m3, a skeletal density of between about 1,000 and about 2,000 kg/m3 and a humidity of between 0 and about 5 wt %. Methods for preparation and use of the additive are also provided. By the use of the additive of the present invention, the hydroconversion process can be performed at high conversion level.
摘要翻译：用于加氢转化方法的添加剂包括具有约0.1至约2,000μm的粒度，约500至约2,000kg / m 3的堆积密度，约1,000至约2,000kg / m 3的骨架密度的固体有机材料和0至约5重量％的湿度。还提供了添加剂的制备和使用方法。通过使用本发明的添加剂，可以以高转化率进行加氢转化处理。

5. 发明申请

US20110174690A1 ADDITIVE FOR HYDROCONVERSION PROCESS AND METHOD FOR MAKING AND USING SAME 有权
标题翻译：加氢方法及其制备方法和使用方法
公开(公告)号：US20110174690A1
公开(公告)日：2011-07-21
申请号：US12691248
申请日：2010-01-21
申请人： Carlos Canelon , Angel Rivas , Omayra Delgado , Miguel Paiva , Giuseppe Di Sarli , Luis Zacarias
发明人： Carlos Canelon , Angel Rivas , Omayra Delgado , Miguel Paiva , Giuseppe Di Sarli , Luis Zacarias
IPC分类号： C10G47/02 , C01B31/02 , B02C19/20
CPC分类号： B01J20/30 , B01J20/3021 , B01J20/3078 , B01J35/0026 , C10G49/10 , C10G2300/205 , C10G2300/4025 , C10G2300/80 , Y10T428/2982
摘要： An additive for hydroconversion processes includes a solid organic material having a particle size of between about 0.1 and about 2,000 μm, a bulk density of between about 500 and about 2,000 kg/m3, a skeletal density of between about 1,000 and about 2,000 kg/m3 and a humidity of between 0 and about 5 wt %. Methods for preparation and use of the additive are also provided. By the use of the additive of the present invention, the hydroconversion process can be performed at high conversion level.
摘要翻译：用于加氢转化方法的添加剂包括具有约0.1至约2,000μm的粒度，约500至约2,000kg / m 3的堆积密度，约1,000至约2,000kg / m 3的骨架密度的固体有机材料和0至约5重量％的湿度。还提供了添加剂的制备和使用方法。通过使用本发明的添加剂，可以以高转化率进行加氢转化处理。

6. 发明申请

US20060289339A1 Method of Hydrogenation of Heavy Oil 失效
标题翻译：重油加氢方法
公开(公告)号：US20060289339A1
公开(公告)日：2006-12-28
申请号：US11426277
申请日：2006-06-23
申请人： Jose Lourenco , Hannu Salokangas
发明人： Jose Lourenco , Hannu Salokangas
IPC分类号： C10G45/00
CPC分类号： B01J8/228 , B01J19/243 , B01J2208/003 , B01J2208/0053 , B01J2208/00575 , B01J2219/00006 , C10G45/00 , C10G47/00 , C10G49/00 , C10G49/10
摘要： A method of hydrogenation of heavy oil. A first step involves providing a continuous pipe reactor defining a serpentine flow path. A second step involves heating heavy oil to lower the viscosity of the heavy oil. A third step involves pumping a turbulent flow of heavy oil and hydrogen through the continuous pipe reactor to promote addition of hydrogen into the heavy oil. The method has improved mass transfer due to the continuous turbulent flow through the continuous pipe reactor.
摘要翻译：重油加氢的方法。第一步涉及提供限定蛇形流动路径的连续管式反应器。第二步涉及加热重油以降低重油的粘度。第三步涉及通过连续管式反应器泵送湍流的重油和氢气，以促进向重油中加入氢气。该方法由于通过连续管式反应器的连续湍流而改善了质量传递。

7. 发明授权

US09850437B2 Enhanced processes to produce value-added products from light gases 有权
公开(公告)号：US09850437B2
公开(公告)日：2017-12-26
申请号：US14463858
申请日：2014-08-20
申请人： H R D Corporation
发明人： Abbas Hassan , Aziz Hassan , Rayford G. Anthony , Gregory G. Borsinger
IPC分类号： C10G49/20 , C10G49/22 , C10G49/10 , C01B3/26 , C10G45/00 , C10G45/02 , C10G45/12 , C10G47/00 , C10G47/24 , C10G50/00 , C10G2/00 , C10G9/00 , B01J8/22 , B01J19/18 , B01F7/00 , B01F13/10 , C01B3/22 , C01B3/24 , C01B3/50
CPC分类号： C10G49/22 , B01F7/00766 , B01F13/1016 , B01J8/222 , B01J19/1806 , B01J2208/00283 , B01J2219/0011 , B01J2219/00189 , C01B3/22 , C01B3/24 , C01B3/26 , C01B3/50 , C01B2203/0272 , C01B2203/0277 , C01B2203/10 , C01B2203/1041 , C01B2203/1235 , C01B2203/1241 , C01B2203/1247 , C01B2203/1276 , C01B2203/148 , C10G2/30 , C10G2/342 , C10G9/00 , C10G45/00 , C10G45/02 , C10G45/12 , C10G47/00 , C10G47/24 , C10G49/10 , C10G49/20 , C10G50/00
摘要： Herein disclosed is a method of producing value-added product from light gases, the method comprising: (a) providing light gases comprising at least one compound selected from the group consisting of C1-C6 compounds and combinations thereof; (b) intimately mixing the light gases with a liquid carrier in a high shear device to form a dispersion of gas in the liquid carrier, wherein the dispersion is supersaturated with the light gases and comprises gas bubbles at least some of which have a mean diameter of less than or equal to about 5 micron(s); (c) allowing the value-added product to form and utilizing vacuum to extract unreacted light gases from the liquid carrier; (d) extracting the value-added product; wherein the value-added product comprises at least one component selected from the group consisting of higher hydrocarbons, hydrogen, olefins, alcohols, aldehydes, and ketones. A system for producing value-added product from light gases is also disclosed.

8. 发明授权

US08192691B2 Hydrocarbon conversion unit including a reaction zone receiving transferred catalyst 有权
标题翻译：烃转化装置包括接收转移的催化剂的反应区
公开(公告)号：US08192691B2
公开(公告)日：2012-06-05
申请号：US12858888
申请日：2010-08-18
申请人： David J. Fecteau , Paul A. Sechrist , Christopher Naunheimer
发明人： David J. Fecteau , Paul A. Sechrist , Christopher Naunheimer
IPC分类号： F27B15/08 , B01J8/08 , C10G35/10
CPC分类号： C10G11/14 , B01J8/125 , B01J2219/00006 , C10G35/10 , C10G49/10 , C10G2300/4012
摘要： One exemplary embodiment can include an apparatus for transferring catalyst from a regeneration zone to a reaction zone in a hydrocarbon conversion unit. The hydrocarbon conversion unit can include a transfer vessel, and first, second, and third lines. The transfer vessel can transfer regenerated catalyst from the regeneration zone at a first pressure to the reaction zone at a second pressure where the second pressure is greater than the first pressure. Generally, the first line communicates the catalyst to the transfer vessel and is coupled to a first valve to allow catalyst into the transfer vessel and the second line communicates the catalyst from the transfer vessel and is coupled to a second valve to allow catalyst out of the transfer vessel. The third line for allowing the passage of gas therethrough may be at a pressure higher than the first pressure having a first portion communicating with the transfer vessel and having a second portion coupled to third and fourth valves. Each of the third and fourth valves can have a first position that is open and a second position that is closed, which may correspond, respectively, to the opening and closing of the first and second valves to allow gas to pass therethrough.
摘要翻译：一个示例性实施例可以包括用于将催化剂从再生区转移到烃转化单元中的反应区的装置。烃转化单元可以包括转移容器，以及第一，第二和第三管线。转移容器可以在第二压力大于第一压力的第二压力下将再生催化剂在第一压力下从再生区转移到反应区。通常，第一管线将催化剂连接到转移容器并且耦合到第一阀以允许催化剂进入转移容器，并且第二管线将催化剂与转移容器连通并且联接到第二阀，以使催化剂脱离转运船。用于允许气体通过的第三条线可以处于比第一压力高的压力，该第一压力具有与转移容器连通的第一部分，并具有连接到第三和第四阀的第二部分。第三阀和第四阀中的每一个可以具有打开的第一位置和关闭的第二位置，其可分别对应于第一和第二阀的打开和关闭以允许气体通过。

9. 发明授权

US07811447B2 Method of transferring particles from one pressure zone to another pressure zone 有权
标题翻译：将颗粒从一个压力区转移到另一个压力区的方法
公开(公告)号：US07811447B2
公开(公告)日：2010-10-12
申请号：US11832059
申请日：2007-08-01
申请人： David J. Fecteau , Christopher Naunheimer
发明人： David J. Fecteau , Christopher Naunheimer
IPC分类号： B01J8/12
CPC分类号： C10G49/10 , B01J8/0015 , B01J8/082 , B01J2219/00207 , B01J2219/00218 , B01J2219/00231 , C10G11/14 , C10G35/10
摘要： One exemplary embodiment can include a method of controlling a catalyst transfer vessel cycle of loading and unloading based on an expected level of a catalyst in a downstream vessel for a hydrocarbon conversion unit. The method can include calculating an expected catalyst level in the downstream vessel based on the unloading of the catalyst transfer vessel to adjust a setpoint to change the catalyst transfer vessel cycle of loading and unloading.
摘要翻译：一个示例性实施方案可以包括基于用于烃转化单元的下游容器中催化剂的预期水平来控制装载和卸载的催化剂转移容器循环的方法。该方法可以包括基于卸载催化剂转移容器来计算下游容器中的预期催化剂含量以调节设定点以改变催化剂转移容器的装载和卸载循环。

10. 发明申请

US20090032440A1 METHOD OF TRANSFERRING PARTICLES FROM ONE PRESSURE ZONE TO ANOTHER PRESSURE ZONE 有权
标题翻译：将颗粒从一个压力区转移到另一个压力区的方法
公开(公告)号：US20090032440A1
公开(公告)日：2009-02-05
申请号：US11832059
申请日：2007-08-01
申请人： David J. Fecteau , Christopher Naunheimer
发明人： David J. Fecteau , Christopher Naunheimer
IPC分类号： B01J8/12
CPC分类号： C10G49/10 , B01J8/0015 , B01J8/082 , B01J2219/00207 , B01J2219/00218 , B01J2219/00231 , C10G11/14 , C10G35/10
摘要： One exemplary embodiment can include a method of controlling a catalyst transfer vessel cycle of loading and unloading based on an expected level of a catalyst in a downstream vessel for a hydrocarbon conversion unit. The method can include calculating an expected catalyst level in the downstream vessel based on the unloading of the catalyst transfer vessel to adjust a setpoint to change the catalyst transfer vessel cycle of loading and unloading.
摘要翻译：一个示例性实施方案可以包括基于用于烃转化单元的下游容器中催化剂的预期水平来控制装载和卸载的催化剂转移容器循环的方法。该方法可以包括基于卸载催化剂转移容器来计算下游容器中的预期催化剂含量以调节设定点以改变催化剂转移容器的装载和卸载循环。

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