OPERATING METHOD FOR FLUID CATALYTIC CRACKING
    22.
    发明申请
    OPERATING METHOD FOR FLUID CATALYTIC CRACKING 审中-公开
    流体催化裂化操作方法

    公开(公告)号:WO9955802A8

    公开(公告)日:2001-04-26

    申请号:PCT/US9908648

    申请日:1999-04-20

    CPC classification number: C10G11/18

    Abstract: The present invention is directed to a Fluid Catalytic Cracking process conducted under fluid catalytic cracking conditions by injecting into at least one reaction zone of a fluid catalytic cracking unit (FCCU) having one or more risers, a plurality of feeds wherein said plurality of feeds comprises at least one feed ( alpha ) and at least another feed ( beta ) wherein said feeds ( alpha ) and ( beta ) (a) differ in Conradson Carbon Residue by at least about 2 wt % points; or (b) differ in hydrogen content by at least about 0.2 wt %; or (c) differ in API gravities by at least about 2 points; or (d) differ in nitrogen content by at least about 50 ppm; or (e) differ in carbon-to-hydrogen ratio by at least about 0.3; or (f) differ in mean boiling point by at least about 200 DEG F; and wherein said feeds ( alpha ) and ( beta ) are alternately injected and wherein said alternate injection maintains said risers in a cyclic steady state, while the rest of the FCC unit is in a steady state.

    Abstract translation: 本发明涉及一种在流化催化裂化条件下进行的流体催化裂化方法,该方法是将具有一个或多个立管的流化催化裂化装置(FCCU)的至少一个反应区注入多个进料,其中所述多个进料包含 至少一种进料(α)和至少另一种进料(β),其中所述进料(α)和(β)(a)在康拉德森碳残余物中不同至少约2重量% 或(b)氢含量不同至少约0.2wt%; 或(c)API重力差异至少约2分; 或(d)氮含量不同至少约50ppm; 或(e)碳 - 氢比率至少约为0.3; 或(f)平均沸点不同至少约200°F; 并且其中所述进料(α)和(β)被交替注入,并且其中所述交替喷射维持所述提升管处于循环稳定状态,而FCC装置的其余部分处于稳定状态。

    PREMIUM WEAR RESISTANT LUBRICANT
    23.
    发明申请
    PREMIUM WEAR RESISTANT LUBRICANT 审中-公开
    高级耐磨润滑剂

    公开(公告)号:WO0014188A3

    公开(公告)日:2000-06-02

    申请号:PCT/US9919360

    申请日:1999-08-24

    CPC classification number: C10G65/043 C10G2400/10

    Abstract: A premium synthetic lubricant having antiwear properties comprises a synthetic isoparaffinic hydrocarbon base stock and an effective amount of at least one antiwear additive. The antiwear additive is preferably at least one of a metal phosphate, a metal dialkyldithiophosphate, a metal dithiophosphate, a metal thiocarbamate, a metal dithiocarbamate, an ethoxylated amine dialkyldithiophosphate and an ethoxylated amine dithiobenzoate. Metal dialkyldithiophosphates are preferred, particularly zincdialkyldithiophosphate (ZDDP). The base stock is derived from a waxy, Fischer-Tropsch synthesized hydrocarbon feed fraction comprising hydrocarbons having an initial boiling point in the range of about 650-750 DEG F, by a process which comprises hydroisomerizing the feed and dewaxing the isomerate. The lubricant may also contain hydrocarbonaceous and synthetic base stock material in admixture with the Fischer-Tropsch derived base stock.

    Abstract translation: 具有抗磨损性能的优质合成润滑剂包括合成异链烷烃基础油料和有效量的至少一种抗磨添加剂。 抗磨添加剂优选为金属磷酸盐,金属二烷基二硫代磷酸盐,金属二硫代磷酸盐,金属硫代氨基甲酸盐,金属二硫代氨基甲酸盐,乙氧基化二烷基二硫代磷酸胺和乙氧基化二硫代苯甲酸胺中的至少一种。 金属二烷基二硫代磷酸盐是优选的,特别是二烷基二硫代磷酸锌(ZDDP)。 基料由包含初始沸点为约650-750°F的烃的蜡状费 - 托合成烃进料馏分通过包含加氢异构化进料和脱蜡异构化物的方法得到。 润滑剂还可以含有与费 - 托衍生的基料混合的含烃和合成基料原料。

    LOW HYDROGEN SYNGAS USING CO2 AND A NICKEL CATALYST
    25.
    发明申请
    LOW HYDROGEN SYNGAS USING CO2 AND A NICKEL CATALYST 审中-公开
    使用二氧化碳和镍催化剂的低氢合成方法

    公开(公告)号:WO9923030A9

    公开(公告)日:1999-08-12

    申请号:PCT/US9823340

    申请日:1998-10-30

    Abstract: A process for making a synthesis gas comprising H2 and CO in the presence of a reforming catalyst comprising a supported non-noble Group VIII metal catalytic component from a feed including a low molecular weight alkane, and preferably methane as in natural gas, O2 H2O and CO2 without catalyst deactivation is achieved by partially oxidizing and steam reforming the feed in the presence of the catalyst. The feed H2O to hydrocarbon carbon mole ratio is less than 2. The mole ratio of the combined feed CO2 and H2O to hydrocarbon carbon ranges from 0.5 - 2.5 and that of the feed H2O to CO2 ranges from 0.35 - 6. Synthesis gas having H2 to CO mole ratios less than 2:1 and even less than 1.5:1 are easily achieved with net CO2 consumption, which also makes the process environmentally beneficial.

    Abstract translation: 一种在重整催化剂存在下制备合成气的方法,所述重整催化剂包含负载的非贵重的第VIII族金属催化组分,所述催化剂组分包括低分子量烷烃,优选天然气中的甲烷,O 2 H 2 O和 没有催化剂失活的CO 2通过在催化剂存在下部分氧化和蒸汽重整进料来实现。 进料H 2 O与烃碳摩尔比小于2.混合进料CO 2和H 2 O与烃碳的摩尔比为0.5-2.5,进料H 2 O至CO 2的摩尔比范围为0.35-6。具有H 2至 CO二氧化碳的比例小于2:1,甚至小于1.5:1即可轻松实现净二氧化碳消耗,这也使得该方法对环境有益。

    DEMETALLIZATION METHOD OF PETROLEUM FLOW

    公开(公告)号:JPH11236576A

    公开(公告)日:1999-08-31

    申请号:JP34593398

    申请日:1998-12-04

    Abstract: PROBLEM TO BE SOLVED: To provide a method with high cost-efficiency for removing a metal from a refinery supply-flow. SOLUTION: A petroleum flow is electrochemically demetallized by contacting a hydrocarbon-soluble metal containing petroleum flow and an aqueous electrolytic medium with a metal cathode having a low hydrogen overvoltage under an electrical current and a pH which allow demetallization of a petroleum flow. The voltage of the cathode is 0 to -3.0 V relative to SCE at a pH of 7-14. The material for the cathode is typically a stainless steel, chromium, copper and nickel.

    REDUCTION IN CONRADSON CARBON VALUE OF PETROLEUM FLOW

    公开(公告)号:JPH11236575A

    公开(公告)日:1999-08-31

    申请号:JP34587498

    申请日:1998-12-04

    Abstract: PROBLEM TO BE SOLVED: To provide a method for reducing a Conradson carbon value of a petroleum flow of a starting material. SOLUTION: A Conradson carbon value of a petroleum flow is electrochemically reduced by contacting a hydrocarbon-soluble Conradson carbon containing petroleum flow and an aqueous electrolytic medium with a metal cathode having a low hydrogen overvoltage under an electrical current and a pH which allow reduction in a Conradson carbon in a petroleum flow. The voltage of the cathode is 0 to -3.0 V relative to SCE at a pH of 7-14. The material for the cathode is typically a stainless steel, chromium, copper and nickel.

    COUNTERCURRENT REACTOR WITH INTERMEDIATE STAGE FOR REMOVING AMMONIA AND HYDROGEN SULFIDE IN GAS-LIQUID CONTACT ZONE

    公开(公告)号:JPH11193386A

    公开(公告)日:1999-07-21

    申请号:JP28880998

    申请日:1998-09-25

    Abstract: PROBLEM TO BE SOLVED: To increase the flow rate of a liquid passing through a reaction bed of a reactor for reacting a liquid flow of petroleum or of a chemical with a treating gas contg. hydrogen in the presence of a catalyst in a countercurrent reaction zone by installing a means for causing at least a part of the treating gas to bypass the reaction zone. SOLUTION: The reactor includes a catalyst bed 4 for causing the reaction between a liquid flow and a treating gas, a nonreaction zone installed in contact with the upstream side of the reaction zone, and a gas-liquid contact zone installed in the nonreaction zone and equipped with an open-structured contact means made of a solid substance. In this reactor, a liquid-introducing means 6 for introducing the unreacted portion of a liquid flow into the reactor is installed at the upper part of the nonreaction zone; a means 8 for leading the unreacted portion of the treating gas to the reactor 1 is installed at the lower part of the reaction zone; a liq. discharge means 10 for discharging the reacted portion of the liquid flow is installed at the lower part of the reaction zone; a means 12 for discharging the reacted portion of the treating gas is installed at the upper part of the nonreaction zone of the reaction zone; and a means 14 for causing the treating gas to bypass the reaction zone is installed along the reaction zone.

    FUEL CELL ELECTRODE WITH CO RESISTANCE

    公开(公告)号:JPH11167926A

    公开(公告)日:1999-06-22

    申请号:JP22796698

    申请日:1998-08-12

    Abstract: PROBLEM TO BE SOLVED: To provide an anode material with CO resistance, capable of oxidizing carbon monoxide by low potential energy, restraining undesirable overvoltage to a minimum, and forming from a stable precursor having platinum particles dispersed in non-stoichiometric hydrogen tungsten bronze. SOLUTION: A tungsten oxide source selected from among a group comprising tungsten peroxide, WO3 , H2 WO4 , WO2 , Na2 WO4 , and a mixture of them is deposited on the surface of platinum particles having a surface area in a range of about 100-500 m /g, a content in a range of about 10-40 wt.%, and a particle size of about 20-30 Å to form a composition, and the tungsten oxide source is reduced under a reducing atmosphere. Platinum carried on carbon, dispersed in non-stoichiometric hydrogen tungsten bronze, capable of depositing on the electrode material can be formed.

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