Zeolitic para-xylene separation with diethyltoluene heavy desorbent
    1.
    发明授权
    Zeolitic para-xylene separation with diethyltoluene heavy desorbent 失效
    用二乙基甲苯重剥离剂进行沸石对二甲苯分离

    公开(公告)号:US5012038A

    公开(公告)日:1991-04-30

    申请号:US389024

    申请日:1989-08-03

    CPC classification number: C07C7/13

    Abstract: A chromatographic process able to separate para-xylene from C.sub.8 isomers and C.sub.9 aromatics. In the process, the para-xylene-containing feed mixture is contacted with an X or Y zeolite adsorbent having Group IA or IIA cations, e.g., barium and/or potassium at exchangeable cationic sites. The para-xylene is selectively adsorbed onto the adsorbent. The feed is then removed from the adsorbent and the para-xylene recovered by desorption with diethyltoluene. The C.sub.9 's and the other xylene isomers in the raffinate, can be separated from this heavy desorbent by fractionation of the raffinate and the desorbent recycled to the process. The preferred desorbents are 2,3-diethyltoluene, 2,5-diethyltoluene and 2,6-diethyltoluene.

    Abstract translation: 可将对二甲苯与C8异构体和C9芳族化合物分离的色谱法。 在该方法中,将含对二甲苯的进料混合物与具有IA或IIA族阳离子的X或Y沸石吸附剂接触,例如可交换阳离子位点的钡和/或钾。 对二甲苯选择性吸附到吸附剂上。 然后从吸附剂中取出进料,通过用二乙基甲苯解吸回收对二甲苯。 萃余液中的C9和其他二甲苯异构体可以通过再循环到该方法的萃余液和解吸剂的分馏而与该重解吸剂分离。 优选的脱附剂是2,3-二乙基甲苯,2,5-二乙基甲苯和2,6-二乙基甲苯。

    Purification of chloroform
    2.
    发明授权
    Purification of chloroform 失效
    氯仿纯化

    公开(公告)号:US4922044A

    公开(公告)日:1990-05-01

    申请号:US267058

    申请日:1988-11-04

    CPC classification number: C07C17/38

    Abstract: Industrial grade chloroform is purified to remove traces of cis-1,2-dichloroethylene, bromochloromethane, and amylenes by a two-step process. The chloroform is first treated by contacting with aqueous sulfuric acid to remove amylenes and thereafter passed over a zeolite having an average pore size of 3 to 6 Angstroms and a Si/Al atomic ratio in the range of about 1.6/1 to 3/1, preferably calcium chabazite, to remove cis-1,2-dichloroethylene and bromochloromethane.

    Abstract translation: 通过两步法纯化工业级氯仿以除去痕量的顺式-1,2-二氯乙烯,溴氯甲烷和戊烯。 氯仿首先通过与硫酸水溶液接触以除去二聚戊烯,然后通过平均孔径为3至6埃的沸石和Si / Al原子比在约1.6 / 1至3/1范围内, 优选钙菱沸石,以除去顺式-1,2-二氯乙烯和溴氯甲烷。

    Separation of indene from alkyl aromatics
    3.
    发明授权
    Separation of indene from alkyl aromatics 失效
    茚与烷基芳烃的分离

    公开(公告)号:US4827077A

    公开(公告)日:1989-05-02

    申请号:US165192

    申请日:1988-02-22

    CPC classification number: B01D15/08 C07C7/13 C07C2102/08

    Abstract: The chromatographic adsorption separation of indene from petrochemical or synthetic feed mixtures with an Na- or K-exchanged X- or Y-zeolite and toluene, benzene, fluorobenzene or other halogen- or alkyl-substituted monocyclic aromatic desorbents. Selectivity of the separation is dependent on water content, from 1-8% (wt.), of the adsorbent.

    Abstract translation: 用Na-或K-交换的X或Y-沸石和甲苯,苯,氟苯或其它卤素或烷基取代的单环芳烃脱附物从石化或合成进料混合物中进行茚的色谱吸附分离。 分离的选择性取决于吸附剂的1-8%(重量)的含水量。

    Process for separating the minor isomers of dinitrotoluene
    4.
    发明授权
    Process for separating the minor isomers of dinitrotoluene 失效
    分离二硝基甲苯的次要异构体的方法

    公开(公告)号:US4717778A

    公开(公告)日:1988-01-05

    申请号:US782345

    申请日:1985-10-01

    CPC classification number: C07C201/16

    Abstract: This invention comprises a process for separating the minor dinitrotoluene isomers, 2,3-dinitrotoluene and 3,4-dinitrotoluene from a feed mixture comprising 2,4- and 2,6-dinitrotoluene, and the minor isomers, which process comprises contacting the mixtures at adsorption conditions with an adsorbent comprising a Y type, or dealuminated Y type, zeolite, cation exchanged with Na, Ca or H, thereby selectively adsorbing the 2,3- and 3,4- isomers or 2,4- and 2-6 isomers, respectively. The remainder of the feed mixture is removed from the adsorbent and the minor isomers are recovered by desorption at desorption conditions with a desorbent material comprising an alcohol, ketone or an ester.

    Abstract translation: 本发明包括从包含2,4-和2,6-二硝基甲苯的进料混合物和次要异构体中分离次要二硝基甲苯异构体,2,3-二硝基甲苯和3,4-二硝基甲苯的方法,该方法包括使混合物 在含有Y型或脱铝Y型沸石,沸石,与Na,Ca或H交换的阳离子的吸附剂的吸附条件下,从而选择性吸附2,3-和3,4-异构体或2,4-和2-6 异构体。 进料混合物的其余部分从吸附剂中除去,并且通过在解吸附条件下用包含醇,酮或酯的解吸剂材料解吸来回收次要异构体。

    Process for separating fatty acids and triglycerides
    5.
    发明授权
    Process for separating fatty acids and triglycerides 失效
    分离脂肪酸和甘油三酸酯的方法

    公开(公告)号:US5102582A

    公开(公告)日:1992-04-07

    申请号:US583269

    申请日:1990-09-17

    CPC classification number: C11B3/10 C11C1/02

    Abstract: The separation of free fatty acids from triglycerides and/or diglycerides is performed by an adsorptive chromatographic process in liquid phase with a crystalline aluminophosphate, e.g., AIPO.sub.4 -5, AIPO.sub.4 -11 or AIPO.sub.4 -54, as the adsorbent. A ketone, having from 3 to 8 carbon atoms, such as 2-heptanone, or a mixture thereof, alone or admixed with a normal alkane can be selected as the desorbent.

    Abstract translation: 游离脂肪酸与甘油三酯和/或甘油二酯的分离是通过与结晶磷酸铝如AIPO4-5,AIPO4-11或AIPO4-54作为吸附剂在液相中的吸附色谱法进行的。 可以选择具有3至8个碳原子的酮,例如2-庚酮或其混合物,单独或与正烷烃混合的酮作为解吸剂。

    Extractive chromatographic separation process for recovering
3,5-diethyltoluene
    6.
    发明授权
    Extractive chromatographic separation process for recovering 3,5-diethyltoluene 失效
    萃取色谱分离方法,用于回收3,5-二乙基甲苯

    公开(公告)号:US5019271A

    公开(公告)日:1991-05-28

    申请号:US443800

    申请日:1989-11-28

    CPC classification number: B01D15/08 B01J20/186 B01J20/281 C07C7/13 B01J2220/56

    Abstract: This invention comprises a process for separating 3,5-diethyltoluene from a feed mixture comprising 3,5-diethyltoluene and at least one isomer thereof, which process comprises contacting the mixture at adsorption conditions with an adsorbent comprising an X zeolite cation exchange with a K cation, thereby selectively adsorbing the 3,5-diethyltoluene. The remainder of the feed mixture is removed by desorption at desorption conditions with a desorbent material comprising a monocyclic alkyl-substituted aromatic hydrocation, e.g., p- or m-diethylbenzene or p-cymene and optionally, a diluent, e.g., isooctane.

    Abstract translation: 本发明包括从包含3,5-二乙基甲苯和至少一种异构体的进料混合物中分离3,5-二乙基甲苯的方法,该方法包括在吸附条件下将混合物与包含X沸石阳离子交换的吸附剂与K 阳离子,从而选择性地吸附3,5-二乙基甲苯。 进料混合物的其余部分通过在解吸条件下通过解吸附材料除去,该解吸材料包含单环烷基取代的芳族烃化反应,例如对 - 或间 - 二乙基苯或对 - 异丙基异丙烯以及任选的稀释剂,例如异辛烷。

    Zeolitic para-xylene separation with tetralin heavy desorbent
    7.
    发明授权
    Zeolitic para-xylene separation with tetralin heavy desorbent 失效
    沸石对二甲苯分离与四氢化萘重解吸剂

    公开(公告)号:US4886930A

    公开(公告)日:1989-12-12

    申请号:US197787

    申请日:1988-05-23

    CPC classification number: C07C7/13

    Abstract: A chromatographic process able to separate para-xylene from C.sub.8 isomers and C.sub.9 aromatics. In the process, the para-xylene-containing feed mixture is contacted with an X or Y zeolite adsorbent having Group IA or IIA cations, e.g., barium and/or potassium, at exchangeable cationic sites. The para-xylene components are selectively adsorbed onto the adsorbent. The non-adsorbed feed is then removed from the adsorbent and the para-xylene recovered by desorption with tetralin. The C.sub.9 's and the other xylene isomers in the raffinate, can be separated from this heavy desorbent by fractionation of the raffinate and the desorbent recycled to the process.

    Abstract translation: 可将对二甲苯与C8异构体和C9芳族化合物分离的色谱法。 在此过程中,将含对二甲苯的进料混合物与具有IA或IIA阳离子的X或Y沸石吸附剂,例如钡和/或钾交换阳离子位置。 对二甲苯组分选择性地吸附到吸附剂上。 然后从吸附剂中除去未吸附的进料,通过用四氢化萘脱附来回收对二甲苯。 萃余液中的C9和其他二甲苯异构体可以通过再循环到该方法的萃余液和解吸剂的分馏而与该重解吸剂分离。

    Zeolitic para-xylene separation with diethyltoluene heavy desorbent
    8.
    发明授权
    Zeolitic para-xylene separation with diethyltoluene heavy desorbent 失效
    用二乙基甲苯重剥离剂进行沸石对二甲苯分离

    公开(公告)号:US4864069A

    公开(公告)日:1989-09-05

    申请号:US197740

    申请日:1988-05-23

    CPC classification number: C07C7/13

    Abstract: A chromatographic process able to separate para-xylene from C.sub.8 isomers and C.sub.9 aromatics. In the process, the para-xylene-containing feed mixture is contacted with an X or Y zeolite adsorbent having Group IA or IIA cations, e.g., barium and/or potassium at exchangeable cationic sites. The para-xylene is selectively adsorbed onto the adsorbent. The feed is then removed from the adsorbent and the para-xylene recovered by desorption with diethyltoluene. The C.sub.9 's and the other xylene isomers in the raffinate, can be separated from this heavy desorbent by fractionation of the raffinate and the desorbent recycled to the process.

    Abstract translation: 可将对二甲苯与C8异构体和C9芳族化合物分离的色谱法。 在该方法中,将含对二甲苯的进料混合物与具有IA或IIA族阳离子的X或Y沸石吸附剂接触,例如可交换阳离子位点的钡和/或钾。 对二甲苯选择性吸附到吸附剂上。 然后从吸附剂中取出进料,通过用二乙基甲苯解吸回收对二甲苯。 萃余液中的C9和其他二甲苯异构体可以通过再循环到该方法的萃余液和解吸剂的分馏而与该重解吸剂分离。

    Process for separating isomers of toluenediamine
    9.
    发明授权
    Process for separating isomers of toluenediamine 失效
    分离甲苯二胺异构体的方法

    公开(公告)号:US4633018A

    公开(公告)日:1986-12-30

    申请号:US811623

    申请日:1985-12-20

    CPC classification number: C07C209/86

    Abstract: This invention comprises a process for separating 2,4-toluenediamine from a feed mixture comprising 2,4-toluenediamine and at least one isomer thereof, which process comprises contacting the mixture at adsorption conditions with an adsorbent comprising a Y type zeolite cation-exchanged with a Ni or Ca cation or an X type zeolite cation-exchanged with a cation from the group Na, Ni and K, thereby selectively adsorbing the 2,4-toluenediamine or an L type zeolite cation-exchanged with a K cation, or an X type zeolite cation exchanged with a Ba cation, thereby selectively adsorbing the 2,6-toluenediamine. The remainder of the feed mixture is removed from the adsorbent and the adsorbed toluenediamine isomer is recovered by desorption at desorption conditions with a desorbent material comprising a lower alcohol or an amine.

    Abstract translation: 本发明包括从包含2,4-甲苯二胺及其至少一种异构体的进料混合物中分离2,4-甲苯二胺的方法,该方法包括使吸附条件下的混合物与包含Y型沸石阳离子交换的Y型沸石 与Na,Ni和K族的阳离子进行阳离子交换的Ni或Ca阳离子或X型沸石,从而选择性吸附2,4-甲苯二胺或与K阳离子交换的L型沸石,或X 型沸石阳离子与Ba阳离子交换,从而选择性吸附2,6-甲苯二胺。 从吸附剂中除去剩余的进料混合物,通过在解吸条件下用包含低级醇或胺的解吸剂材料解吸来回收吸附的甲苯二胺异构体。

    Process for separating isomers of toluidine
    10.
    发明授权
    Process for separating isomers of toluidine 失效
    分离甲苯胺异构体的方法

    公开(公告)号:US4480129A

    公开(公告)日:1984-10-30

    申请号:US537123

    申请日:1983-09-29

    CPC classification number: C07C209/86

    Abstract: This invention comprises a process for separating p-toluidine from a feed mixture comprising p-toluidine and o- or m-toluidine, which process comprises contacting the mixture at adsorption conditions with an adsorbent comprising an X or Y-type zeolite cation exchanged with a cation in the group Fe, Mn, Co, Ni or Zn, thereby selectively adsorbing the p-toluidine. The remainder of the feed mixture is removed from the adsorbent and the p-toluidine is recovered by desorption at desorption conditions with a desorbent material comprising aniline or an alkyl amine excluding alkyl amines having eight or more carbon atoms per molecule when the adsorbent comprises an X-type zeolite.

    Abstract translation: 本发明包括从包含对甲苯胺和邻 - 或间甲苯胺的进料混合物中分离对甲苯胺的方法,该方法包括在吸附条件下将混合物与包含与下式交换的X或Y型沸石阳离子的吸附剂接触: Fe,Mn,Co,Ni或Zn组中的阳离子,从而选择性吸附对甲苯胺。 进料混合物的其余部分从吸附剂中除去,并且在脱附条件下用解吸附物质回收对甲苯胺,当包含苯胺或烷基胺的解吸剂材料除去每分子具有八个或更多个碳原子的烷基胺时,当吸附剂包含X 型沸石。

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