公开(公告)号：US20160137937A1

公开(公告)日：2016-05-19

申请号：US14898004

申请日：2014-06-19

Applicant: ARGENT ENERGY GROUP LIMITED

Inventor： Michael Scott

IPC: C10L1/02

CPC classification number: C10L1/026 ,  B01D21/262 ,  B03D1/1431 ,  C07C67/03 ,  C07C67/08 ,  C07C67/58 ,  C10G3/00 ,  C10G3/40 ,  C10G33/00 ,  C10G2300/1003 ,  C10G2300/201 ,  C10G2400/04 ,  C10L2200/0446 ,  C10L2200/0476 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/06 ,  C10L2290/18 ,  C10L2290/542 ,  C10L2290/543 ,  C10L2290/544 ,  C10L2290/547 ,  C11B3/001 ,  C11B3/006 ,  C11B3/008 ,  C11B3/04 ,  C11B3/12 ,  C11B3/16 ,  C11C3/003 ,  C11C3/10 ,  Y02E50/13 ,  Y02P30/20 ,  C07C69/24 ,  C07C69/52

Abstract: There is described a biodiesel composition and process for producing biodiesel and related products. There is also described related fuels and fuel blends comprising biodiesel. The biodiesel composition may be prepared from a mixture comprising fats, oils and greases from sewer waste.

Abstract translation: 描述了用于生产生物柴油及相关产品的生物柴油组合物和方法。 还描述了包含生物柴油的相关燃料和燃料混合物。 生物柴油组合物可以由包含来自下水道废物的脂肪，油和油脂的混合物制备。

公开(公告)号：US20160137936A1

公开(公告)日：2016-05-19

申请号：US14897815

申请日：2014-06-19

Applicant: ARGENT ENERGY GROUP LIMITED

Inventor： Michael Scott

IPC: C10L1/02 ,  C11B3/16 ,  C11B3/00

CPC classification number: C10L1/026 ,  B01D21/262 ,  B03D1/1431 ,  C07C67/03 ,  C07C67/08 ,  C07C67/58 ,  C10G3/00 ,  C10G3/40 ,  C10G33/00 ,  C10G2300/1003 ,  C10G2300/201 ,  C10G2400/04 ,  C10L2200/0446 ,  C10L2200/0476 ,  C10L2270/026 ,  C10L2270/04 ,  C10L2290/06 ,  C10L2290/18 ,  C10L2290/542 ,  C10L2290/543 ,  C10L2290/544 ,  C10L2290/547 ,  C11B3/001 ,  C11B3/006 ,  C11B3/008 ,  C11B3/04 ,  C11B3/12 ,  C11B3/16 ,  C11C3/003 ,  C11C3/10 ,  Y02E50/13 ,  Y02P30/20 ,  C07C69/24 ,  C07C69/52

Abstract: There is described a process and an apparatus for purifying a mixture and related products. In particular, there is described a process and an apparatus for purifying a mixture comprising fats, oils and greases as are typically found in sewer waste. The process involves heating, acidifying and separating the mixture. The apparatus used includes a heating and separation device for separating into a solid fraction, an organic liquid fraction and an aqueous liquid fraction. Apparatus such as a three phase separation unit and a rotary vacuum filter may also be used.

Abstract translation: 描述了用于纯化混合物和相关产品的方法和装置。 特别地，描述了用于纯化通常在下水道废物中发现的包含脂肪，油和油脂的混合物的方法和设备。 该方法包括加热，酸化和分离混合物。 使用的装置包括用于分离成固体部分，有机液体部分和含水液体部分的加热和分离装置。 还可以使用诸如三相分离单元和旋转真空过滤器的设备。

公开(公告)号：US09328295B2

公开(公告)日：2016-05-03

申请号：US14039003

申请日：2013-09-27

Applicant: UOP LLC

Inventor： Rajeswar R. Gattupalli ,  Beckay J. Mezza ,  Alakananda Bhattacharyya ,  Carl J. Stevens ,  Joao Jorge da Silva Ferreira Alves ,  Massimo Sangalli

IPC: C10G21/28 ,  B01D11/04 ,  C10G21/06

CPC classification number: C10G21/28 ,  B01D11/04 ,  B01D11/0426 ,  B01D11/0446 ,  C10G21/06 ,  C10G2300/201 ,  C10G2300/4056 ,  C10G2300/4081

Abstract: Recycle of an extract stream containing a contaminant is used to improve recovery of hydrocarbons in a contaminant removal process. At least a portion of an extract stream is recycled to a contaminant extraction zone and contacted with rich ionic liquid. Contaminants in the recycle extract stream are transferred to the rich ionic liquid.

Abstract translation: 使用含有污染物的提取物流的回收利用来改善污染物去除过程中碳氢化合物的回收。 至少一部分提取物流被再循环到污染物提取区并与富离子液体接触。 再循环提取物流中的污染物被转移到富离子液体中。

公开(公告)号：US09242190B2

公开(公告)日：2016-01-26

申请号：US12960215

申请日：2010-12-03

Applicant: James W. Patten

Inventor： James W. Patten

IPC: B01D15/00 ,  B01J20/02 ,  B01J20/22

CPC classification number: B01D15/00 ,  B01J20/02 ,  B01J20/22 ,  B01J2220/4887 ,  B01J2220/56 ,  C10G2300/201

Abstract: A method of removing fines from a hydrocarbon-containing fluid can include preparing a bed media of particulate earthen material (12). The hydrocarbon-containing fluid having fines therein can be passed through the bed media (12) at a flow rate such that a portion of the fines are retained in the bed media (12) to form a filtered hydrocarbon-containing fluid. The flow rate is sufficient to maintain a wetting film of the hydrocarbon-containing fluid across at least a majority portion of the particulate earthen material which is contacted by the hydrocarbon-containing fluid. The filtered hydrocarbon-containing fluid can be recovered from the bed media (12) via a suitable outlet (16) having substantially reduced or eliminated fines content.

Abstract translation: 从含烃流体中除去细粉的方法可包括制备颗粒状土壤材料（12）的床介质。 其中具有细粉的含烃流体可以以使得一部分细粒保留在床介质（12）中以形成过滤的含烃流体的流速通过床介质（12）。 流速足以使含烃流体的湿润膜保持在与含烃流体接触的至少大部分颗粒状土层材料中。 过滤的含烃流体可以通过具有显着减少或消除的细粉含量的合适出口（16）从床介质（12）中回收。

公开(公告)号：US20160002122A1

公开(公告)日：2016-01-07

申请号：US14857068

申请日：2015-09-17

Applicant: TOTAL RESEARCH & TECHNOLOGY FELUY

Inventor： Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

IPC: C07C1/24 ,  C08F10/02 ,  C12P7/16 ,  C07C4/06 ,  C07C6/04

CPC classification number: C07C1/24 ,  B01J29/40 ,  B01J2229/42 ,  C07C1/22 ,  C07C4/06 ,  C07C6/04 ,  C07C2529/40 ,  C08F10/02 ,  C10G3/42 ,  C10G3/44 ,  C10G3/49 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/22 ,  C12P5/026 ,  C12P7/16 ,  Y02E50/10 ,  Y02P20/52 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/08 ,  C07C11/06

Abstract: A process for the conversion of an alcohol mixture to make propylene may include introducing into a reactor a stream that includes the alcohol mixture. The alcohol mixture may include 20 to 100 weight percent isobutanol. The process may include contacting the stream with a single catalyst at a temperature above 450° C. in the reactor at conditions effective to dehydrate the isobutanol, forming C4+ olefins, and to catalytically crack the C4+ olefins. The single catalyst may be an acid catalyst adapted to cause both the dehydration and the catalytic cracking. The process may include recovering from the reactor an effluent that includes ethylene, propylene, water, and various hydrocarbons. The process may include fractionating the effluent to produce an ethylene stream, a propylene stream, a fraction of hydrocarbons having 4 carbon atoms or more, and water.

公开(公告)号：US09228139B2

公开(公告)日：2016-01-05

申请号：US13847918

申请日：2013-03-20

Applicant: Raheel Shafi ,  Abdennour Bourane ,  Abdul Rahman Zafer Akhras ,  Essam Sayed ,  Ibrahim A. Abba

Inventor： Raheel Shafi ,  Abdennour Bourane ,  Abdul Rahman Zafer Akhras ,  Essam Sayed ,  Ibrahim A. Abba

IPC: C10G69/06 ,  C10G9/00 ,  C10G51/06 ,  C10G9/16 ,  C10B57/04 ,  C10G49/00 ,  C10G69/00 ,  C10G9/14

CPC classification number: C10G69/06 ,  C10B57/045 ,  C10G9/005 ,  C10G9/16 ,  C10G49/007 ,  C10G51/06 ,  C10G69/00 ,  C10G2300/201 ,  C10G2300/308 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30 ,  Y02P20/132

Abstract: An integrated hydrotreating, steam pyrolysis and coker process for the direct processing of a crude oil is provided to produce olefinic and aromatic petrochemicals, and petroleum coke. Crude oil and recycled coker liquid product are charged to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent which is thermally cracked in the presence of steam to produce a mixed product stream. The residual liquid fraction recovered upstream of the thermal cracking unit or within the thermal cracking unit is thermally cracked under conditions effective to produce coke and coker liquid product. The coker liquid product is recycled to the step of hydroprocessing while the petroleum coke is recovered. Hydrogen from the mixed product stream is purified and recycled to the hydroprocessing zone, and olefins, aromatics and pyrolysis fuel oil are recovered from the separated mixed product stream.

Abstract translation: 提供了一种用于直接加工原油的综合加氢处理，蒸汽热解和焦化工艺，以生产烯烃和芳香族石油化学品和石油焦炭。 将原油和再循环焦化液体产物装入加氢处理区，该加氢处理区在有效地产生加氢处理流出物的条件下运行，该加氢处理流出物在蒸汽存在下被热裂解以产生混合产物流。 在热裂解单元上游或在热裂解装置中回收的剩余液体馏分在有效生产焦炭和焦化液体产物的条件下被热裂解。 在回收石油焦时，将焦化液体产物再循环至加氢处理步骤。 将来自混合产物流的氢气纯化并再循环至加氢处理区，并从分离的混合产物流中回收烯烃，芳烃和热解燃料油。

公开(公告)号：US20150330166A1

公开(公告)日：2015-11-19

申请号：US14808180

申请日：2015-07-24

Applicant: Joe D. MICKLER ,  Lance STANFILL

Inventor： Joe D. MICKLER ,  Lance STANFILL

IPC: E21B21/06

CPC classification number: E21B21/065 ,  B09B3/00 ,  B09C1/00 ,  B09C1/02 ,  B09C1/06 ,  C10G1/045 ,  C10G2300/201 ,  C10G2300/44 ,  E21B21/066

Abstract: A method and apparatus for removing and recovering oil from wellbore cuttings is provided. Oil-contaminated solids are transported through two or more solvent baths on vibrating conveyors and contacted with solvent flowing countercurrent to the direction of transport of the oil-contaminated solids through the baths such that oil contaminant is separated from the solids.

Abstract translation: 提供了一种用于从井眼切屑中除去和回收油的方法和装置。 油污染的固体通过两个或更多个在振动输送机上的溶剂浴进行输送，并与溶剂流接触，该溶剂与被油污染的固体的运输方向逆流通过浴，使得油污染物与固体分离。

公开(公告)号：US20150225311A1

公开(公告)日：2015-08-13

申请号：US14694282

申请日：2015-04-23

Applicant: TOTAL RESEARCH & TECHNOLOGY FELUY

Inventor： Cindy Adam ,  Delphine Minoux ,  Nikolai Nesterenko ,  Sander Van Donk ,  Jean-Pierre Dath

IPC: C07C1/24 ,  C12P7/16 ,  C07C6/04

CPC classification number: C07C1/24 ,  B01J29/40 ,  B01J2229/42 ,  C07C1/22 ,  C07C4/06 ,  C07C6/04 ,  C07C2529/40 ,  C08F10/02 ,  C10G3/42 ,  C10G3/44 ,  C10G3/49 ,  C10G2300/1014 ,  C10G2300/1022 ,  C10G2300/201 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/22 ,  C12P5/026 ,  C12P7/16 ,  Y02E50/10 ,  Y02P20/52 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/08 ,  C07C11/06

Abstract: A process for the conversion of an alcohol mixture to make propylene may include introducing into a reactor a stream that includes the alcohol mixture. The alcohol mixture may include 20 to 100 weight percent isobutanol. The process may include contacting the stream with a single catalyst at a temperature above 450° C. in the reactor at conditions effective to dehydrate the isobutanol, forming C4+ olefins, and to catalytically crack the C4+ olefins. The single catalyst may be an acid catalyst adapted to cause both the dehydration and the catalytic cracking. The process may include recovering from the reactor an effluent that includes ethylene, propylene, water, and various hydrocarbons. The process may include fractionating the effluent to produce an ethylene stream, a propylene stream, a fraction of hydrocarbons having 4 carbon atoms or more, and water.

Abstract translation: 将醇混合物转化成丙烯的方法可包括向反应器中引入包含醇混合物的流。 醇混合物可以包括20至100重量％的异丁醇。 该方法可以包括在反应器内在高于450℃的温度下将流与单一催化剂接触，所述条件有效地使异丁醇脱水，形成C4 +烯烃，并催化裂解C4 +烯烃。 单一催化剂可以是适于引起脱水和催化裂化两者的酸催化剂。 该方法可以包括从反应器中回收包含乙烯，丙烯，水和各种烃的流出物。 该方法可以包括将流出物分馏以产生乙烯流，丙烯流，具有4个碳原子或更多个碳原子的部分和水。

公开(公告)号：US20150129461A1

公开(公告)日：2015-05-14

申请号：US14080269

申请日：2013-11-14

Applicant: UOP LLC

Inventor： Soumendra Mohan Banerjee

IPC: C10G65/04

CPC classification number: C10G65/04 ,  C10G65/16 ,  C10G69/04 ,  C10G69/06 ,  C10G2300/201

Abstract: Embodiments of apparatuses and methods for hydrotreating coker kerosene or other thermally or catalytically cracked hydrocarbon stream are provided. In one example, a method comprises splitting a feed comprising coker kerosene into first and second feed streams. The first feed stream is heated to form a heated first feed stream. The second feed stream is partially heated to form a partially heated second feed stream. The heated first feed stream is contacted with a first hydrotreating catalyst to form a first hydrotreated intermediate stream. The first hydrotreated intermediate stream is combined with the partially heated second feed stream to form a partially quenched first hydrotreated intermediate combined stream. The partially quenched first hydrotreated intermediate combined stream is contacted with a second hydrotreating catalyst to further hydrotreat the partially quenched first hydrotreated intermediate combined stream.

Abstract translation: 提供了用于加氢精炼焦煤或其他热或催化裂化烃流的装置和方法的实施方案。 在一个实例中，一种方法包括将包含焦化煤油的进料分成第一和第二进料流。 将第一进料流加热以形成加热的第一进料流。 第二进料流被部分加热以形成部分加热的第二进料流。 加热的第一进料流与第一加氢处理催化剂接触以形成第一加氢处理的中间流。 将第一加氢处理的中间物流与部分加热的第二进料流合并以形成部分骤冷的第一加氢处理的中间混合料流。 将部分骤冷的第一加氢处理的中间混合料流与第二加氢处理催化剂接触以进一步加氢部分骤冷的第一加氢处理的中间混合料流。

公开(公告)号：US08992766B2

公开(公告)日：2015-03-31

申请号：US13163204

申请日：2011-06-17

Applicant: Tushar V. Choudhary ,  Walter E. Alvarez ,  Joseph E. Bares

Inventor： Tushar V. Choudhary ,  Walter E. Alvarez ,  Joseph E. Bares

IPC: C10G47/00 ,  C10G11/18 ,  C10G47/36 ,  G01N33/28

CPC classification number: C10G11/187 ,  C10G47/36 ,  C10G2300/1044 ,  C10G2300/1055 ,  C10G2300/201 ,  C10G2300/301 ,  C10G2300/305 ,  C10G2300/308 ,  C10G2400/02 ,  C10G2400/04 ,  G01N33/2823

Abstract: A method of upgrading naphtha and diesel yields from fluid catalytic cracking and hydrocracking units by improving a feed quality of a petroleum feedstock, product or fraction mixture. The method of improving the feed quality of the petroleum feedstock, product or fraction mixture occurs by first determining the API Gravity of a petroleum feedstock, product or fraction mixture. A temperature at which about fifty percent of the petroleum feedstock, product or fraction boils (T50) is then determined. The feed quality for the petroleum feedstock, product or fraction mixture as determined from the API Gravity and the T50 for the feedstock, product or fraction mixture is then estimated followed by adjusting the petroleum feedstock, product or fraction mixture to achieve a higher feed quality.

Abstract translation: 通过提高石油原料，产物或级分混合物的进料质量来提高来自流化催化裂化和加氢裂化装置的石脑油和柴油产率的方法。 通过首先确定石油原料，产物或级分混合物的API重力来改善石油原料，产物或级分混合物的进料质量的方法。 然后测定约50％的石油原料，产物或部分沸腾（T50）的温度。 然后估计从API Gravity和原料，产物或级分混合物的T50确定的石油原料，产物或级分混合物的进料质量，然后调整石油原料，产物或级分混合物以获得更高的进料质量。