Purification of hf catalyst in alkylation process
    1.
    发明授权
    Purification of hf catalyst in alkylation process 失效
    高效催化剂在烷基化工艺中的纯化

    公开(公告)号:US3793264A

    公开(公告)日:1974-02-19

    申请号:US3793264D

    申请日:1971-12-01

    Inventor: CHAPMAN C

    CPC classification number: C01B7/195 B01J27/32 Y02P20/584

    Abstract: OLEFINS AND ISOPARAFFINS ARE ALKYLATED IN THE PRESENCE OF AN HF CATALYST. THE REACTOR EFFLUENT IS PASSED TO A SETTLING ZONE. THE HYDROCARBON PHASE IS FRACTIONATED TO RECOVER AN ALKYLATE PRODUCT. THE ACID PHASE IS RECYCLED TO THE REACTOR. A PORTION OF THE RECYCLED ACID IS PASSED TO A PURIFICATION COLUMN FOR REMOVAL OF ACID SOLUBLE OIL. STRIP-

    PING VAPOR IS INTRODUCED INTO THE PURIFICATION COLUMN BOTH ABOVE AND BELOW THE SURFACE OF SAID SOLUBLE OIL ACCUMULATED THEREIN. BAFFLES ARE POSITIONED IN THE LOWER REGION OF THE COLUMN TO INCREASE THE VAPOR-LIQUID CONTACTING.

    Fractionator and method of fractionating
    2.
    发明授权
    Fractionator and method of fractionating 失效
    分割器和分割方法

    公开(公告)号:US3856629A

    公开(公告)日:1974-12-24

    申请号:US26136872

    申请日:1972-06-09

    Inventor: CHAPMAN C

    CPC classification number: B01D3/14

    Abstract: An improved fractionator and method for separating a hydrocarbon feed stream into first, second, and third component streams by passing the feed stream through an upper chamber of a vessel in indirect heat exchange relationship with separated first and second upper chambers of the vessel which are in fluid communication with a lower portion of the vessel. Said first and second upper chambers and said lower chamber have a multiplicity of spaced-apart fractionating trays extending thereacross.

    Abstract translation: 一种改进的分馏器和方法,用于通过使进料流通过容器的上室与间隔热交换关系将烃进料流分离成第一,第二和第三组分流,分离的第一和第二组分流在分离的第一和第二上室中, 与容器的下部流体连通。 所述第一和第二上部腔室和所述下部腔室具有多个在其上延伸的间隔开的分级塔板。

    Treating alkylate-containing hydrocarbon with hf in a unitary vessel
    3.
    发明授权
    Treating alkylate-containing hydrocarbon with hf in a unitary vessel 失效
    在机组中处理含有氢氟酸的含烯烃的烃

    公开(公告)号:US3825616A

    公开(公告)日:1974-07-23

    申请号:US17758671

    申请日:1971-09-03

    Inventor: CHAPMAN C

    CPC classification number: C07C2/62 B01J27/32 C07C2527/1206 Y02P20/584

    Abstract: UPON SEPARATION OF AN ALKYLATION EFFLUENT FROM AN ISOPARAFFIN-OLEFIN HYDROGEN FLUORIDE ALKYLATION INTO A HYDROCARBON PHASE AND AN ACID PHASE, THE HYDROCARBON PHASE, CONTAINING ORGANIC FLUORIDES, IN CONTACTED WITH RELATIVELY PURE HF RESULTING FROM A RERUN OR PURIFACTION OF HF IN THE PRESENCE OF ISOPARAFFIN WHICH ACTS TO CONVERT AND, THEREFORE, TO REDUCE ORGANIC FLUORIDE CONTENT OF THE HF BEING RERUN. ADDITIONAL RERUN HF SUBSTANTIALLY FREE FROM OR HAVING A CNSIDERABLY REDUCED ORGANIC FLUORIDE CONTENT CAN BE USED TO FURTHER REDUCE ORGANIC FLUORIDE IN SAID HYDROCARBON PHASE.

    Purification of hf catalyst in alkylation process

    公开(公告)号:US3793394A

    公开(公告)日:1974-02-19

    申请号:US3793394D

    申请日:1972-05-08

    Inventor: CHAPMAN C

    Abstract: OLEFINS AND ISOPARAFFINS ARE ALKYLATED IN THE PRESENCE OF AN HF CATALYST. REACTOR EFFLUENT IS PASSED TO A SETTLING ZONE. THE HYDROCARBON PHASE IS FRACTIONATED TO RECOVER AN ALKYLATE PRODUCT. THE ACID PHASE IS RECYCLED TO THE REACTOR. A PORTION OF THE RECYCLED ACID IS PASSED TO A PURIFICATION COLUMN FOR REMOVAL OF ACID SOLUBLE OIL. STRIPPING VAPOR AND REFLUX LIQUID ARE PASSED TO THE PURIFICATION COLUMN TO REMOVE SUBSTANTIALLY ALL OF THE HF FROM THE ACID SOLUBLE OIL. A SUBSTANTIAL PORTION OF THE ACID SOLUBLE OIL REMOVED FROM THE PURIFICATION COLUMN IS CONTACTED EXTERNALLY WITH STRIPPING VAPOR AND REINTRODUCED INTO THE PURIFICATION COLUMN.

    Treatment of propane in hf alkylation with purified hf
    5.
    发明授权
    Treatment of propane in hf alkylation with purified hf 失效
    用纯化HF处理HF碱性中的丙烷

    公开(公告)号:US3767727A

    公开(公告)日:1973-10-23

    申请号:US3767727D

    申请日:1971-09-01

    Inventor: CHAPMAN C

    CPC classification number: C07C2/62 C07C2527/1206 Y10S585/905

    Abstract: IN AN ALKYLATION OF AN ISOPARAFFIN WITH AN OLEFIN, A LIGHT HYDROCARBON PHASE, E.G., A PROPANE PHASE AND AN ACID PHASE, BOTH PHASES CONTAINING ORGANIC FLUORIDE, ARE RECOVERED UPON FRACTIONATION OF THE ALKYLATION REACTION EFFLUENT, THE ACID PHASE IS CONTACTED WITH ISOPARAFFIN TO REACT OUT ORGANIC FLUORIDE, ISOPARAFFIN PHASE AND ACID PHASE ARE THUS OBTAINED, THE ISOPARAFFIN PHASE CONTAINING ALKYLATE PRODUCED FROM THE ORGANIC FLUORIDE, THE ACID PHASE NOW

    CONTAINING RELATIVELY LESS ORGANIC FLUORIDE THEN BEING ADMIXED WITH THE LIGHT HYDROCARBON OR PROPANE CONTAINING PHASE, THUS REMOVING INTO THE ACID ORGANIC FLUORIDE IN SAID PHASE WHEREUPON THE ACID PHASE IS REACTED WITH ISOPARAFFIN TO PRODUCE ADDITIONAL ALKYLATE FROM THE ORGANIC FLUORIDE.

    Method for removing alkyl fluoride from an alkylation admixture in a riser reaction zone
    6.
    发明授权
    Method for removing alkyl fluoride from an alkylation admixture in a riser reaction zone 失效
    从上升反应区的碱性化合物中除去氟化亚烷基的方法

    公开(公告)号:US3763264A

    公开(公告)日:1973-10-02

    申请号:US3763264D

    申请日:1971-04-30

    Inventor: CHAPMAN C

    Abstract: ALKYL FLUORIDE IN ISORARAFFIN-OLEFIN ALKYLATE PRODUCED IN PRESENCE OF HF CATALYST, E.G., AN ALKYLATE PRODUCED BY ALKYLATING ISOPARAFFIN WITH ETHYLENE AND ISOBUTYLENE OR PROPYLENE WITH AN HF CATALYST, IS CAUSED TO ALKYLATE AN ISOPARAFFIN IN THE PRESENCE OF ADDITIONAL HF ACID CATALYST BY PASSING THE ALKYLATE UPWARDLY THROUGH NOZZLES INTO A RISER-REACTOR AND AT THE NOZZLES ADMIXING WITH THE ALKYLATE OF ADDITIONAL HF ACID OF A DESRABLE KIND IN A DESIBRABLE QUANTITY TO CAUSE CONVERSION OF THE ALKYL FLUORIDE TO ADDITIONAL ALKYLATE, THE APPARATUS IN WHICH THE INVENTION IS CARRIED OUT ESSENTIALLY BEING COMPOSED OF A VESSEL HAVING A LOWER, A MID AND UPPER SECTIONS, A RISER-REACTOR CONDUIT BEING JUXTAPOSED OVER HYDROCARBON SPRAY NOZZLES IN A PARTITION BETWEEN THE LOWER AND MID SECTIONS, BUT NOT EXTENDING DOWN TO SIAD PARTITION, A SECOND CONDUIT SURROUNDING THE RISER-REACTOR CONDUIT EXTENDING FROM SAID PARTION TO AN APERTURED PARTITION BETWEEN THE MID AND UPPER SECTIONS, SIAD SECOND CONDUIT AT ITS UPPER END BEING IN SEALING ENGAGEMENT WITH SAID APERTURED PARTION AND IN REGISTER WITH THE APERTURE THEREIN, SAID RISER CONDUIT EXTENDING TO A LEVEL ABOVE SIAD APERTURED PARTION, AND DOWNCOMER MEANS FOR FLOWING ACID FROM SAID UPPER SECTION TO SAID LOWER SECTION, DOWNCOMER MEANS FOR FLOWING

    HYDROCARBON FROM SAID UPPER SECTION, IN ONE EMBODIMENT, INTO A HYDROCARBON SURGE SECTION SURROUNDING SAID SECOND CONDUIT AND BETWEEN SAID PARTITIONS, AND MEANS FOR FEEDING ALKYLATE TO SAID LOWER SECTION AND FORCEFULLY UPWARDLY THROUGH SAID NOZZLES. IN ANOTHER EMBODIMENT AN ANGULAR SYSTEM COMPRISES RIGH ANGLED CONDUITS, AN ACID FLOW DIVERTER OVER HYDROCARBON PASSAGE TO DIVERT DOWN FLOWING ACID FROM AN OPENING TO PERMIT HYDROCARBON TO FLOW ESSENTIALLY HORIZONTALLY THROUGH SAID OPENING IS DESCRIBED.

    Process and apparatus for maintaining a divided accumulator
    7.
    发明授权
    Process and apparatus for maintaining a divided accumulator 失效
    用于维护分散式累加器的过程和装置

    公开(公告)号:US3822193A

    公开(公告)日:1974-07-02

    申请号:US18347271

    申请日:1971-09-24

    Inventor: CHAPMAN C

    CPC classification number: C10G33/06 B01D3/14 C07C7/04

    Abstract: A METHOD IS PROVIDED WHEREBY LIQUID PARAFFIN IS ACCUMULATED AND DISTRIBUTED FROM A VESSEL DIVIDED INTERNALLY BY A WEIR, SO THAT TWO DISPARATE STREAMS CAN BE MAINTAINED IN THE VESSEL WITH MIXING OF INLET MATERIALS ON ON SIDE OF THE WEIR WHILE MAINTAINING AN UNMIXED MATERIAL ON THE OTHER SIDE OF THE WIRE. IN ONE EMBODIMENT OF THE INVENTION ISOBUTANE REFLUX LIQUID IS MAINTAINED ON ONE SIDE OF THE WEIR AND OVERFLOWED INTO A SECOND ZONE WHERE IT IS MIXED WITH THE WET EFFLUENT FROM A FEED STREAM DRIER WHICH CONTAINS ISOBUTANE, OLEFINS, AND WATER. FEED WATER IS TRAPPED FROM THE MIXED STREAM AND DECANTED FROM THIS ZONE.

    Hf alkylation system utilizing alkylate stream reboil
    10.
    发明授权
    Hf alkylation system utilizing alkylate stream reboil 失效
    高效碱性系统利用碱性物流

    公开(公告)号:US3857904A

    公开(公告)日:1974-12-31

    申请号:US35761573

    申请日:1973-05-07

    Inventor: CHAPMAN C

    CPC classification number: C07C2/62 C07C7/005 C07C2527/1206 C07C9/16

    Abstract: A side draw stream from an isostripper to a debutanizer is removed from the isostripper as a liquid stream of normal butane and higher hydrocarbons. The alkylate-containing bottoms fromthe isostripper are used to indirectly heat or reboil the bottom of the debutanizer. Alkylate is recovered from the reboiler line as well as from the debutanizer.

    Abstract translation: 从等离子体捕捉剂到脱丁烷剂的侧馏分流作为正丁烷和高级烃的液体流从等压捕集器中除去。 来自等离子体捕获器的含烷基化物的底部物质用于间接加热或再沸腾脱丁器的底部。 从再沸器管线以及脱丁烷塔中回收烷基化物。

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