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    SYNGAS CONVERSION AND CATALYST SYSTEM EMPLOYED THEREFOR
    51.
    发明申请
    SYNGAS CONVERSION AND CATALYST SYSTEM EMPLOYED THEREFOR 审中-公开
    其使用的SYNGAS转换和催化剂体系

    公开(公告)号：WO2003089392A1

    公开(公告)日：2003-10-30

    申请号：PCT/US2002/028262

    申请日：2002-09-05

    Applicant: PHILLIPS PETROLEUM COMPANY ,  WU, An-hsiang ,  YAO, Jianhua ,  DRAKE, Charles, A.

    Inventor： WU, An-hsiang ,  YAO, Jianhua ,  DRAKE, Charles, A.

    IPC: C07C27/00

    CPC classification number: C07C41/01 ,  B01J23/80 ,  B01J29/084 ,  B01J29/85 ,  B01J35/0006 ,  C07C1/20 ,  C07C2529/85 ,  C07C11/02 ,  C07C43/043

    Abstract: A process for the conversion of syngas by contact of syngas under conversion conditions with catalyst having as components zinc oxide, copper oxide, aluminium oxide, Y zeolite and clay in which (A) in a one step process for conversion of syngas to dimethyl ether, the catalyst has as components an extruded mixture of zinc oxide, copper oxide, gamma aluminum oxide, Y zeolite and clay; (B) in a two step process for conversion of syngas to light olefins, a catalyst system is employed that has in the first step a catalyst mixture of zinc oxide, copper oxide, aluminum oxide, Y zeolite and clay and the catalyst employed in the second step is SAPO-34; SAPO-34 modified with lanthanum (III) nitrate hexahydrate; SAPO-34 modified with magnesium nitrate hexahydrate; SAPO-34 modified with tributyl borate or SAPO-34 modified with triethyl phosphate or (C) in a two step process for conversion of syngas to light olefins, the pressure on the effluent from the contact of syngas with a mixture of zinc oxide, copper oxide, aluminium oxide, Y zeolite and clay is reduced before contact with a second catalyst of SAPO-34. The catalyst systems employed in the processes herein.

    Abstract translation: 在合成气与转化条件下的合成气与作为组分的氧化锌，氧化铜，氧化铝，Y沸石和粘土的催化剂的转化合成气的方法，其中（A）在合成气转化为二甲醚的一步法中， 催化剂具有氧化锌，氧化铜，γ氧化铝，Y沸石和粘土的挤出混合物的组分; （B）在将合成气转化为轻质烯烃的两步法中，采用了催化剂体系，该催化剂体系在第一步中是氧化锌，氧化铜，氧化铝，Y沸石和粘土的催化剂混合物， 第二步是SAPO-34; 用硝酸镧（III）六水合物修饰的SAPO-34; SAPO-34用硝酸镁六水合物改性; 用硼酸三丁酯或用三乙基磷酸酯改性的SAPO-34改性的SAPO-34或（C）在合成气转化为轻质烯烃的两步法中，合成气与氧化锌，铜的混合物接触的流出物的压力 氧化物，氧化铝，Y沸石和粘土在与SAPO-34的第二催化剂接触之前还原。 本文工艺中使用的催化剂体系。

    IMPROVED CATALYTIC REFORMING PROCESS
    53.
    发明申请
    IMPROVED CATALYTIC REFORMING PROCESS 审中-公开
    改进的催化改性方法

    公开(公告)号：WO2003000827A1

    公开(公告)日：2003-01-03

    申请号：PCT/US2001/019607

    申请日：2001-06-20

    Applicant: PHILLIPS PETROLEUM COMPANY ,  LIN, Fan-Nan ,  PARSONS, John, S.

    Inventor： LIN, Fan-Nan ,  PARSONS, John, S.

    IPC: C10G35/04

    CPC classification number: B01J23/6567 ,  B01J23/90 ,  C10G35/04 ,  C10G35/085 ,  C10G35/09

    Abstract: A substantially water-free hydrocarbon feed is charged to a reformer reactor operated under reforming conditions, thereafter, a chlorine-containing additive is introduced, without the simultaneous introduction of water, into the substantially water-free hydrocarbon feed being charged to the reformer reactor in an amount and for a time period that are effective to inhibit deactivation of the reformer catalyst; thereafter, the introduction of the chlorine-containing additive is terminated and the charging of the substantially water-free hydrocrbon feed to the reformer reactor is continued.

    Abstract translation: 将基本上无水的烃进料加入到在重整条件下操作的重整器反应器中，然后将不含同时引入的含氯添加剂引入到重整器反应器中的基本上不含水的烃进料中 有效抑制重整器催化剂失活的量和时间段; 此后，终止含氯添加剂的引入，并且继续向重整器反应器充入基本上无水的氢溴酸盐进料。

    SYSTEM FOR DRILLING AND COMPLETING MULTILATERAL WELLS
    54.
    发明申请
    SYSTEM FOR DRILLING AND COMPLETING MULTILATERAL WELLS 审中-公开
    钻孔和完井多孔井系统

    公开(公告)号：WO1998057031A1

    公开(公告)日：1998-12-17

    申请号：PCT/US1997009995

    申请日：1997-06-09

    Applicant: PHILLIPS PETROLEUM COMPANY ,  ALLEN, David, Wayne

    Inventor： PHILLIPS PETROLEUM COMPANY

    IPC: E21B43/14

    CPC classification number: E21B43/305 ,  E21B7/061 ,  E21B41/0042 ,  E21B43/10 ,  E21B43/14

    Abstract: The time required for establishing a multilateral well is reduced by enlarging a section of a wellbore and running a multilateral tool (7) which includes a preassembled combination of casing sections that form dual casing strings extending from the primary casing. The multilateral tool (7) incorporates a carrier section (2), a lateral section (8), and a main section (5). The tool is run with the lateral section (8) releasably held in coaxial alignment within the carrier section (2), and with the main section (5) fixed to the lower end of the carrier section (2). Once in place, the lateral section (8) is released and diverted out of a preformed window (4) in the lower end of the carrier section (2) and runs generally parallel to the main casing section (5). A lateral junction is thus formed at the carrier section window (4) in which dual casing strings are connected to the primary casing. A second window, preformed in the upper end of lateral section (8) is aligned with the bore of the primary casing when the lateral casing section is fully extended out of the carrier section window (4), thus permitting recovery of a diverting device incorporated in the carrier casing section (2) through the second window. The dual strings are then individually drilled and completed with pressure integrity between the dual strings maintained by using straddle equipment across the lateral junction.

    Abstract translation: 通过扩大井筒的一部分并运行多边工具（7）来减少建立多边井所需的时间，其中包括预先组装的套管部分，这些套管部分形成从主套管延伸的双套管。 多边工具（7）包括承载部分（2），横向部分（8）和主要部分（5）。 该工具以可移动地保持在承载部分（2）内同轴对准的横向部分（8）运行，并且主部分（5）固定到承载部分（2）的下端。 一旦就位，横向部分（8）被释放并从承载部分（2）的下端中的预制窗口（4）转出并且大致平行于主壳体部分（5）延伸。 因此，在载体部分窗口（4）处形成横向接头，其中双壳体连接到主壳体。 当横向壳体部分完全延伸出承载部分窗口（4）之后，在侧部（8）的上端中预成型的第二窗口与主壳体的孔对准，从而允许回收包含的转向装置 在载体壳体部分（2）中通过第二窗口。 然后单独钻出双列，并通过横跨横向结合使用跨越设备保持的双重串之间的压力完整性完成。

    PROCESS FOR REDUCING SALT CONTENT IN A HYDROCARBON CONTAINING FLUID
    56.
    发明申请
    PROCESS FOR REDUCING SALT CONTENT IN A HYDROCARBON CONTAINING FLUID 审中-公开
    含有液体油中盐含量的方法

    公开(公告)号：WO1997029169A1

    公开(公告)日：1997-08-14

    申请号：PCT/US1997000406

    申请日：1997-01-08

    Applicant: PHILLIPS PETROLEUM COMPANY ,  MITCHELL, Kent, Edward

    Inventor： PHILLIPS PETROLEUM COMPANY

    IPC: C10G17/04

    CPC classification number: C10G31/08

    Abstract: A process for desalting a crude oil comprises (1) injecting steam into the oil to form a steam-injected oil; (2) adding water to the steam-injected oil to form a mixture; (3) introducing the mixture to a desalter; (4) inducing the formation of aqueous phase and oil phase; and (5) separating the oil phase from the aqueous phase. Where there are two desalting stages for desalting crude oil, the process can be carried out in either the first stage or second stage, or both stages. The process can also be similarly employed in a multistage desalting process.

    Abstract translation: 用于脱盐原油的方法包括（1）将蒸汽注入油中以形成蒸汽注入的油; （2）向蒸汽注入的油中加入水以形成混合物; （3）将混合物引入脱盐器; （4）引起水相和油相的形成; 和（5）将油相与水相分离。 在脱盐原油有两个脱盐阶段的情况下，该过程可以在第一阶段或第二阶段或两个阶段进行。 该方法也可类似地用于多级脱盐方法。

    PROCESS FOR PREPARING POLYOLEFINS HAVING A BIMODAL MOLECULAR WEIGHT DISTRIBUTION
    58.
    发明申请
    PROCESS FOR PREPARING POLYOLEFINS HAVING A BIMODAL MOLECULAR WEIGHT DISTRIBUTION 审中-公开
    制备具有双重分子量分布的聚烯烃的方法

    公开(公告)号：WO1992015619A1

    公开(公告)日：1992-09-17

    申请号：PCT/US1992001820

    申请日：1992-03-03

    Applicant: PHILLIPS PETROLEUM COMPANY

    Inventor： PHILLIPS PETROLEUM COMPANY ,  STRICKLEN, Phil, Marvin

    IPC: C08F02/38

    CPC classification number: C08F297/08 ,  C08F210/00 ,  C08F210/16 ,  C08F2/001 ,  C08F210/14 ,  C08F2500/05 ,  C08F2500/12

    Abstract: A two-step polymerization process for producing a polyolefin having a bimodal molecular weight distribution is provided. In step one, under polymerization conditions, at least two different alpha-olefins are contacted with a catalyst system which comprises an aluminoxane and a metallocene, selected from the group consisting of mono, di, and tri-cyclopentadienyls and substituted cyclopentadienyls, of a metal selected from titanium, vanadium, chromium, zirconium, niobium, molybdenum, hafnium, tantalum, and tungsten, provided however if said metal is titanium then a metallocene of at least one other of said metals is present such that a first polymerization mixture is formed which comprises a low crystallinity, high molecular weight, copolymer, unreacted monomer, unreacted comonomer, and catalyst. This is followed by contacting, under polymerization conditions, hydrogen (and optionally additional alpha-olefin), with said first polymerization mixture which comprises copolymer, unreacted monomer, unreacted comonomer, and catalyst, such that a second polymerization mixture is formed which comprises a low crystallinity, high molecular weight copolymer, and a high crystallinity, low molecular weight homopolymer.

    Abstract translation: 提供了一种用于制备具有双峰分子量分布的聚烯烃的两步聚合方法。 在步骤1中，在聚合条件下，至少两种不同的α-烯烃与催化剂体系接触，所述催化剂体系包含铝氧烷和选自单，二和三环戊二烯基和取代的环戊二烯基的茂金属，金属 但是，如果所述金属是钛，则提供钛，钒，铬，锆，铌，钼，铪，钽和钨的金属，然后存在至少另一种所述金属的茂金属，使得形成第一聚合混合物， 包含低结晶度，高分子量，共聚物，未反应单体，未反应的共聚单体和催化剂。 然后在聚合条件下使氢（和任选地另外的α-烯烃）与包含共聚物，未反应单体，未反应的共聚单体和催化剂的所述第一聚合混合物接触，使得形成第二聚合混合物，其包含低 结晶度，高分子量共聚物和高结晶度低分子量均聚物。

    59.
    发明专利
    未知

    公开(公告)号：ES2041250T3

    公开(公告)日：1993-11-16

    申请号：ES87104253

    申请日：1987-03-23

    Applicant: PHILLIPS PETROLEUM COMPANY

    Inventor： KITCHEN, ALONZO GENE ,  SZALLA, FRANK JOHN

    IPC: C08F4/08 ,  C08F4/42 ,  C08F4/48 ,  C08F297/04 ,  C08L53/00 ,  C08L53/02

    Abstract: Sequential charging of initiator and monomers in a multistage solution polymerization process involving conjugated diene and monovinylaromatic monomers wherein the final charge is a mixture of these monomers results in the production of resinous polymodal linear block copolymers each with a terminal tapered block. A typical 5-stage charge sequence is as follows: Stage 1: (Si); Stage 2: (Si); Stage 3: (B); Stage 4: (Si); Stage 5: (S+B) wherein (Si) is monovinylaromatic monomer and initiator; (B) is conjugated diene monomer and (S+B) is monovinylaromatic monomer and conjugated diene monomer. At each stage, polymerization is allowed to continue until no free monomer is present. The trimodal block copolymer products comprise high, medium and low molecular weight species designated, respectively, as S1-S2-B1-S3-B2->S4; S2-B1-S3-B2->S4; and S3-B2->S4 wherein S1, S2 and S3 represent, respectively, polyvinylaromatic blocks resulting from polymerization of the first, second and third charges of monovinylaromatic monomer (stages 1,2 and 4); B1 represents a polydiene block resulting from polymerization of the first charge of conjugated diene monomer (stage 3); and B2->S4 represents a terminal tapered copolymer block resulting from polymerization of the conjugated diene and monovinylaromatic monomers (stage 5). The subject copolymers can be fabricated into sheets and molded objects possessing little color, a high degree of transparency and excellent impact resistance. These fabricated products do not craze on being impacted.

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