公开(公告)号：WO2017040119A1

公开(公告)日：2017-03-09

申请号：PCT/US2016/048191

申请日：2016-08-23

Applicant: PHILLIPS 66 COMPANY

Inventor： INGRAM, David, B. ,  RANDOLPH, Bruce, B. ,  LOESCHER, Mitchell, E. ,  GUPTA, Alo, K. ,  PAUL, Uchenna, P. ,  LAFRANCOIS, Chris, J. ,  MCDANIEL, Neal, D. ,  SMITH, Danielle, K. ,  BIERSCHENK, David, M. ,  HE, Ting

IPC: H01M4/13 ,  H01M4/131 ,  H01M4/86 ,  H01M8/0258 ,  H01M8/04 ,  H01M8/06 ,  H01M8/1246

CPC classification number: C25B3/02 ,  C25B9/08 ,  C25B11/0478 ,  C25B13/04 ,  C25B15/08

Abstract: The current embodiment describes a process of flowing an oxidant species over the reducing side of an oxygen transport membrane. O 2- anions are then continuously transported from the reducing side through the oxygen transport membrane to the oxidizing side where an organic compound is converted to a partially oxidized organic compound on the oxidizing side.

Abstract translation: 目前的实施方案描述了使氧化剂物质在氧传输膜的还原侧上流动的过程。 然后，将阴离子从还原侧通过氧传输膜连续输送到氧化侧，在氧化侧将有机化合物转化为氧化侧的部分氧化的有机化合物。

公开(公告)号：WO2014204946A1

公开(公告)日：2014-12-24

申请号：PCT/US2014/042717

申请日：2014-06-17

Applicant: PHILLIPS 66 COMPANY ,  KELLER, Alfred E.

Inventor： KELLER, Alfred E.

IPC: C01B17/04

CPC classification number: C01B17/021 ,  B01D5/0012 ,  C01B17/0404 ,  C01B17/0439

Abstract: A horizontal sulfur condenser may include an exterior casing with a plurality of condenser tubes arranged longitudinally within the casing, a liquid sulfur reservoir at a longitudinal end within the exterior casing, and an internal baffle that protrudes into the liquid sulfur reservoir from the surface. The lowest of the plurality of condenser tubes is parallel to a wall of the exterior casing. A Claus process gas inlet is proximate a first end of the plurality of condenser tubes, which are arranged horizontally but are positioned vertically above the sulfur reservoir. A liquid sulfur outlet is located at the liquid sulfur surface. The baffle creates multiple chambers above the sulfur reservoir, such as a first chamber defined by the exterior casing and the baffle to receive condensed Claus sulfur in the liquid reservoir, and a second chamber defined by the exterior casing and the baffle to receive degassed liquid sulfur.

Abstract translation: 水平硫冷凝器可以包括外壳，其具有在壳体内纵向布置的多个冷凝器管，在外壳内的纵向端部处的液体硫储存器，以及从表面突出到液体硫储存器中的内部挡板。 多个冷凝器管中的最下部平行于外壳的壁。 克劳斯工艺气体入口靠近多个冷凝器管的第一端，其水平布置，但位于硫储存器上方的垂直上方。 液体硫出口位于液硫表面。 挡板在硫储存器上方产生多个室，例如由外壳和挡板限定的第一室，以在液体储存器中容纳冷凝的克劳斯硫，以及由外壳和挡板限定的第二室，以接收脱气的液体硫 。

公开(公告)号：WO2014043052A1

公开(公告)日：2014-03-20

申请号：PCT/US2013/058857

申请日：2013-09-10

Applicant: PHILLIPS 66 COMPANY ,  INGRAM, David B. ,  PAUL, Uchenna P.

Inventor： INGRAM, David B. ,  PAUL, Uchenna P.

IPC: H01M8/18 ,  H01M8/06

CPC classification number: F23L7/007 ,  B01D53/047 ,  B01D53/76 ,  B01D2256/16 ,  B01D2257/504 ,  C01B3/38 ,  C01B3/384 ,  C01B2203/0233 ,  C01B2203/0283 ,  C01B2203/043 ,  C01B2203/1241 ,  C25B1/00 ,  C25B1/04 ,  C25B15/08 ,  F23C9/00 ,  F23J2215/40 ,  F23J2215/50 ,  F23L7/005 ,  Y02E20/322 ,  Y02E20/344 ,  Y02E60/366 ,  Y02P20/152

Abstract: A process of producing a feed from a solid oxide electrolysis cell. A first portion of the flue gas produced from a combustion process is directed to the anode side of the solid oxide electrolysis cell. The feed and a second portion of the flue gas are then mixed to produce an enhanced feed. The enhanced feed is then mixed with fuel and combusted in the combustion process to produce flue gas. The flue gas comprises greater than 50 wt% CO 2 and less than 1 wt% N 2 .

Abstract translation: 从固体氧化物电解槽生产原料的方法。 从燃烧过程产生的烟道气的第一部分被引导到固体氧化物电解池的阳极侧。 然后将进料和烟道气的第二部分混合以产生增强的进料。 然后将增强的进料与燃料混合并在燃烧过程中燃烧以产生烟道气。 烟气包括大于50重量％的CO 2和小于1重量％的N 2。

公开(公告)号：WO2014040034A1

公开(公告)日：2014-03-13

申请号：PCT/US2013/058968

申请日：2013-09-10

Applicant: PHILLIPS 66 COMPANY ,  DAUGAARD, Daren E. ,  JONES, Samuel T. ,  GORKE, Johnathan T.

Inventor： DAUGAARD, Daren E. ,  JONES, Samuel T. ,  GORKE, Johnathan T.

IPC: C10B53/02 ,  C10B53/08 ,  C10B57/06 ,  C10G1/08

CPC classification number: C10J3/46 ,  C10B43/14 ,  C10B49/16 ,  C10B53/02 ,  C10B53/08 ,  C10B57/06 ,  C10G1/08 ,  C10G2/32 ,  C10G2300/1011 ,  C10L3/08 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P20/145 ,  Y02P30/20

Abstract: The present disclosure relates generally to a biomass pyrolysis process wherein entrainment of char and other contaminants with the pyrolysis vapors is decreased as a direct consequence of the biomass feedstock comprising particles that are larger than a defined minimum diameter (>300 microns) and preferably less than 1250 microns. The biomass feedstock may optionally be compressed to form feedstock pellets that are larger than this defined minimum diameter.

Abstract translation: 本公开一般涉及生物质热解方法，其中焦炭和其它污染物与热解蒸气的夹带作用减少，因为生物质原料包括大于限定的最小直径（> 300微米）且优选小于 1250微米。 生物质原料可任选地被压缩以形成大于该限定的最小直径的原料颗粒。

公开(公告)号：WO2014031295A1

公开(公告)日：2014-02-27

申请号：PCT/US2013/052719

申请日：2013-07-30

Applicant: PHILLIPS 66 COMPANY ,  HUANG, Hui

Inventor： HUANG, Hui

IPC: C07D277/68

CPC classification number: C07D513/04 ,  C07D277/68

Abstract: A process comprising the step of synthesizing 2,6-dibromo-4,8-dihexylbenzo[1,2-d:4,5-d']bis(thiazole) from 2,5-dihyxylbenzene-1,4-diamine.

Abstract translation: 一种包括从2,5-二羟基苯-1,4-二胺合成2,6-二溴-4,8-​​二己基苯并[1,2-d：4,5-d']双（噻唑）的步骤的方法。

公开(公告)号：WO2013154742A1

公开(公告)日：2013-10-17

申请号：PCT/US2013/031356

申请日：2013-03-14

Applicant: PHILLIPS 66 COMPANY ,  LORD, III, Charles, John ,  NEWLAND, John, Stephen

Inventor： LORD, III, Charles, John ,  NEWLAND, John, Stephen

IPC: G01N27/00

CPC classification number: G01N27/4166 ,  G01N27/08 ,  G01N33/1893 ,  H01M8/026 ,  H01M8/0297 ,  H01M8/10

Abstract: Systems and methods relate to measuring ammonium bisulfide concentration in a fluid sample. The system includes an electrolytic conductivity cell, a temperature sensor and an analyzer. Logic of the analyzer determines the ammonium bisulfide concentration based on signals received from the conductivity cell and the temperature sensor that are coupled to monitor the fluid.

Abstract translation: 系统和方法涉及测量流体样品中二硫化铵浓度。 该系统包括电解电导池，温度传感器和分析仪。 分析仪的逻辑基于从电导池和连接到监测流体的温度传感器接收的信号来测定二硫化铵浓度。

公开(公告)号：WO2013103515A1

公开(公告)日：2013-07-11

申请号：PCT/US2012/070315

申请日：2012-12-18

Applicant: PHILLIPS 66 COMPANY ,  LIU, Shetian ,  YAO, Jianhua ,  XU, Xiaochun ,  BLOSSER, Patrick W. ,  ALLISON, Joe D. ,  SUGHRUE, Edward L. II

Inventor： LIU, Shetian ,  YAO, Jianhua ,  XU, Xiaochun ,  BLOSSER, Patrick W. ,  ALLISON, Joe D. ,  SUGHRUE, Edward L. II

IPC: C07C2/04

CPC classification number: C07C2/24 ,  C10G50/00 ,  C10G2300/1092 ,  C10G2400/02 ,  C10G2400/10

Abstract: Methods and systems relate to upgrading light olefins, such as ethylene, propylene and butylenes, diluted in a gas mixture, such as refinery fuel gas. The upgrading yields products in a gasoline, distillate, lube oil or wax range without requiring purification or compression of the gas mixture prior to feeding the gas mixture to a reactor. In operation, the mixture contacts a solid oligimerization catalyst, such as silica supported chromium, within the reactor. This contact occurs at a first temperature suitable to produce oligomers that are formed of the olefins and adsorb on the catalyst in liquid or solid phases. Next, heating the catalyst to a second temperature higher the first temperature desorbs the oligomers that are recovered and separated into the products.

Abstract translation: 方法和系统涉及在诸如炼油厂燃料气体的气体混合物中稀释的轻质烯烃，例如乙烯，丙烯和丁烯。 升级产生汽油，馏出物，润滑油或蜡的产品，而不需要在将气体混合物送入反应器之前对气体混合物进行纯化或压缩。 在操作中，混合物在反应器内接触固体寡聚化催化剂，例如二氧化硅负载的铬。 该接触在适于产生由烯烃形成并以液相或固相吸附在催化剂上的低聚物的第一温度下进行。 接下来，将催化剂加热至高于第一温度的第二温度，第一温度将回收并分离成产物的低聚物解吸附。

公开(公告)号：WO2013055541A1

公开(公告)日：2013-04-18

申请号：PCT/US2012/058390

申请日：2012-10-02

Applicant: PHILLIPS 66 COMPANY ,  LATIMER, Edward G. ,  SCHUETTE, George F. ,  AICHELE, Clint P. ,  LOESCHER, Mitchell E. ,  HEALD, Randall L.

Inventor： LATIMER, Edward G. ,  SCHUETTE, George F. ,  AICHELE, Clint P. ,  LOESCHER, Mitchell E. ,  HEALD, Randall L.

IPC: B01D53/40 ,  B01D53/77 ,  F22D11/00 ,  F23J15/00 ,  F23J15/04

CPC classification number: B01D53/40 ,  B01D53/485 ,  B01D53/56 ,  B01D53/77 ,  B01D2258/0283 ,  F22B37/008 ,  F23J15/04 ,  F23J15/06 ,  F23J2219/40 ,  F23J2219/70 ,  Y02P80/154

Abstract: Methods for removing acid gases and recovering water from flue gas. A flue gas is introduced into a water spray tower and is cooled by direct contact with a sprayed aqueous stream to condense a portion of the water vapor in the flue gas. Acid gases present in the flue gas are absorbed into the aqueous mixture, and a chemical added to the stream facilitates conversion of absorbed acid gases. The aqueous stream leaving the spray tower is next treated to remove contaminants, such as carbonates and bicarbonates, thereby producing a cleaned aqueous stream that may be split into a stream that is cooled prior to reuse in the spray tower, as well as a stream that is fed back to the boiler.

Abstract translation: 从烟气中除去酸性气体和回收水的方法。 将烟道气引入喷水塔中，并通过与喷射的水流直接接触来冷却烟气中的一部分水蒸气。 存在于烟道气中的酸性气体被吸收到含水混合物中，并且添加到流中的化学物质有利于被吸收的酸性气体的转化。 离开喷雾塔的水流接下来被处理以除去诸如碳酸盐和碳酸氢盐之类的污染物，从而产生清洁的水流，其可以分裂成在喷雾塔中重新使用之前冷却的物流，以及流 被反馈到锅炉。

公开(公告)号：AU2010333904B2

公开(公告)日：2015-05-07

申请号：AU2010333904

申请日：2010-10-26

Applicant: PHILLIPS 66 COMPANY

Inventor： YAO JIANHUA ,  SUGHRUE II EDWARD L ,  BAO YUN ,  FJARE KRISTI ,  SHI TIEPAN

IPC: C07C1/00

Abstract: Materials and processes for the conversion of carbohydrates and polyols to gasoline boiling range hydrocarbons. Carbohydrates and polyols are reacted in the presence of modified zeolite catalysts to form a reaction product containing non-aromatic and aromatic gasoline boiling range hydrocarbons.

公开(公告)号：WO2023091153A1

公开(公告)日：2023-05-25

申请号：PCT/US2021/060340

申请日：2021-11-22

Applicant: PHILLIPS 66 COMPANY

Inventor： NIELSEN, Laura ,  EISENHART, Reed ,  SUDING, Victoria ,  PAN, Hualong ,  CHINEN-MENDEZ, Alyssa

IPC: C08G61/00 ,  C08L65/00 ,  H01L51/54

Abstract: A method of reacting (I) with (II) to produce (III). In this method Y1 and Y2 are independently selected from the group consisting of: H, Cl, Br, I, and combinations thereof. Additionally in this method M is selected from the group consisting of H, trialkylstannane, boronate, or ZnX, wherein X is Cl, Br, or I. Furthermore in this method Z is a divalent linking group selected from the group consisting of: (IV), (V), (VI), (VII), or (VIII). Lastly, in this method R1 is selected from: H, unsubstituted or substituted branched alkyls with 1 to 60 carbon atoms or unsubstituted or substituted linear alkyls with 1 to 60 carbon atoms.