Purification of alpha naphthol-containing feedstock by adsorption
    21.
    发明授权
    Purification of alpha naphthol-containing feedstock by adsorption 失效
    通过吸附纯化含有α-萘酚的原料

    公开(公告)号:US4962273A

    公开(公告)日:1990-10-09

    申请号:US264707

    申请日:1988-10-31

    CPC classification number: C07C37/82

    Abstract: An adsorptive separation process useful in the purification of alpha naphthol-containing feed mixtures, said process comprising the employment of a type X, type Y or a de-aluminated type Y zeolite material and a desorbent material comprising a primary alcohol or an alkyl ester.

    Abstract translation: 用于纯化含有α-萘酚的进料混合物的吸附分离方法,所述方法包括使用X型,Y型或脱铝Y型沸石材料和包含伯醇或烷基酯的解吸材料。

    Process for separating mono-, di- and triglycerides
    22.
    发明授权
    Process for separating mono-, di- and triglycerides 失效
    分离单,二和甘油三酸酯的方法

    公开(公告)号:US4797233A

    公开(公告)日:1989-01-10

    申请号:US898300

    申请日:1986-08-20

    CPC classification number: C11B7/00 B01D15/00 C07C67/56 C11B3/10

    Abstract: The separation of monoglycerides from diglycerides and triglycerides is performed by an adsorptive chromatographic process in liquid phase using sodium, magnesium, lithium or potassium-exchanged X zeolites or potassium or sodium-exchanged Y zeolite, or potassium-exchanged L zeolite as the adsorbent. A ketone or ketone/n-aliphatic hydrocarbon can be selected as the desorbent.

    Abstract translation: 通过使用钠,镁,锂或钾交换的X沸石或钾或钠交换的Y沸石或钾交换的L沸石作为吸附剂,通过液相中的吸附色谱法进行甘油二酯和甘油三酸酯的分离。 可以选择酮或酮/正脂族烃作为解吸剂。

    Process for separating di- and triglycerides
    23.
    发明授权
    Process for separating di- and triglycerides 失效
    分离甘油二酯和甘油三酸酯的方法

    公开(公告)号:US4770819A

    公开(公告)日:1988-09-13

    申请号:US70748

    申请日:1987-07-06

    CPC classification number: C11B7/0008

    Abstract: The separation of diglycerides from triglycerides is performed by an adsorptive chromatographic process in liquid phase with Li-, K-, or hydrogen-exchanged omega zeolites or silica as the adsorbent. A ketone/n-aliphatic hydrocarbon mixture can be selected as the desorbent.

    Abstract translation: 甘油三酸酯从甘油三酸酯中分离是通过吸附色谱法在液相中与Li-,K-或氢交换的ω-沸石或二氧化硅作吸附剂进行的。 可以选择酮/正脂族烃混合物作为解吸剂。

    Process for separating 2,4-toluene diisocyanate from isomers of toluene
diisocyanate
    24.
    发明授权
    Process for separating 2,4-toluene diisocyanate from isomers of toluene diisocyanate 失效
    从甲苯二异氰酸酯异构体中分离2,4-甲苯二异氰酸酯的方法

    公开(公告)号:US4721806A

    公开(公告)日:1988-01-26

    申请号:US47953

    申请日:1987-05-08

    CPC classification number: C07C263/20

    Abstract: This invention comprises a process for separating 2,4-toluene diisocyanate from a feed mixture with 2,6-toluene diisocyanate. The process comprises contacting the mixture at adsorption conditions with an adsorbent comprising a Y-type zeolite cation exchanged with a cation in the group Na, Ca, Li or Mg, thereby selectively adsorbing the 2,4-toluene diisocyanate. The remainder of the feed mixture is removed from the adsorbent and the adsorbed toluene diisocyanate isomer is recovered by desorption at desorption conditions with a desorbent material comprising toluene.

    Abstract translation: 本发明包括用2,6-甲苯二异氰酸酯从进料混合物中分离2,4-甲苯二异氰酸酯的方法。 该方法包括使吸附条件下的混合物与包含与Na,Ca,Li或Mg组中的阳离子交换的Y型沸石阳离子的吸附剂接触,从而选择性吸附2,4-甲苯二异氰酸酯。 进料混合物的其余部分从吸附剂中除去,吸附的甲苯二异氰酸酯异构体通过在解吸条件下用包含甲苯的解吸剂材料解吸来回收。

    Process for separating isomers of dinitrotoluene
    25.
    发明授权
    Process for separating isomers of dinitrotoluene 失效
    分离二硝基甲苯异构体的方法

    公开(公告)号:US4642397A

    公开(公告)日:1987-02-10

    申请号:US782674

    申请日:1985-10-01

    CPC classification number: C07C201/16

    Abstract: This invention comprises a process for separating 2,4-dinitrotoluene from a feed mixture comprising 2,4-dinitrotoluene and at least one isomer thereof, 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 K, Na, Ca, Ba, Li or Mg, thereby selectively adsorbing the 2,4-dinitrotoluene. The remainder of the feed mixture is removed from the adsorbent and the 2,4-dinitrotoluene is recovered by desorption at desorption conditions with a desorbent material comprising a C.sub.3 to C.sub.5 alcohol, a ketone, toluene, an ester or a nitrocompound.

    Abstract translation: 本发明包括从包含2,4-二硝基甲苯和至少一种异构体的进料混合物中分离2,4-二硝基甲苯的方法,该方法包括使吸附条件下的混合物与包含X或Y型沸石阳离子交换的吸附剂接触 在K,Na,Ca,Ba,Li或Mg族中具有阳离子,从而选择性地吸附2,4-二硝基甲苯。 进料混合物的其余部分从吸附剂中除去,2,4-脱硝基甲苯通过在脱附条件下通过解吸附物质包含C 3至C 5醇,酮,甲苯,酯或硝基化合物来回收。

    Zeolitic capillary columns for gas chromatography
    26.
    发明授权
    Zeolitic capillary columns for gas chromatography 失效
    用于气相色谱的沸石毛细管柱

    公开(公告)号:US5719322A

    公开(公告)日:1998-02-17

    申请号:US730719

    申请日:1996-09-20

    CPC classification number: G01N30/56 G01N2030/025 G01N2030/567

    Abstract: Methods have been found to prepare fused silica capillary gas chromatographic columns where the stationary phase is a molecular sieve affixed to the silica capillary wall without the aid of an organic binder by modifying the interior surface of the silica prior to contact with the molecular sieve. These totally inorganic columns greatly expand the application and range of gas chromatographic separations and allow the use of non-traditional carrier gases, even air, while not degrading the separation of components. The columns are films of small molecular sieve particles affixed to a silica surface modified by such treatments as hydrogen peroxide, alumina deposition, or silica deposition followed by fixation at 80.degree.-160.degree. C.

    Abstract translation: 已经发现制备熔融石英毛细管气相色谱柱的方法,其中固定相是通过在与分子筛接触之前改性二氧化硅的内表面而借助于有机粘合剂而附着在二氧化硅毛细管壁上的分子筛。 这些全无机柱大大扩展了气相色谱分离的应用范围,并允许使用非传统载气,甚至空气,同时不会降低组分的分离。 柱是附着在通过诸如过氧化氢,氧化铝沉积或二氧化硅沉积的处理改性的二氧化硅表面上的小分子筛颗粒的膜,随后在80℃-160℃下固定。

    Process for separating para-xylene from a C.sub.8 and C.sub.9 aromatic
mixture
    27.
    发明授权
    Process for separating para-xylene from a C.sub.8 and C.sub.9 aromatic mixture 失效
    从C8和C9芳族混合物中分离对二甲苯的方法

    公开(公告)号:US5177295A

    公开(公告)日:1993-01-05

    申请号:US812262

    申请日:1991-12-23

    CPC classification number: C07C7/13

    Abstract: In the process flow scheme for chromatographically separating para-xylene from C.sub.8 isomers containing substantial amounts of C.sub.9 aromatic hydrocarbon impurities with BaX or KY zeolite adsorbent and heavy desorbents, e.g., tetralin and diethyltoluene, a bottoms stream from the extract fractionation column containing desorbent is recycled to the separation unit and a sidecut stream, containing C.sub.9 aromatic hydrocarbon impurities and a minor amount of the desorbent from the raffinate stream, is directed to the raffinate fractionation column, thereby removing C.sub.9 aromatic hydrocarbons from the desorbent before recycling the desorbent to the separation unit, and preventing C.sub.9 aromatics from building up in the desorbent input. A fractionator for the extract column bottoms stream is eliminated, lowering capital costs, and energy requirements for the raffinate column are reduced.

    Abstract translation: 在使用BaX或KY沸石吸附剂和重质解吸剂(例如四氢化萘和二乙基甲苯)含有大量C 9芳族烃杂质的C8异构体色谱分离对二甲苯的方法流程图中,将含有脱附剂的萃取分馏塔的塔底物流回收 将分离单元和含有C9芳族烃杂质和少量来自萃余液流的解吸剂的侧流引导至萃余液分馏塔,从而在将解吸剂再循环到分离单元之前从解吸剂中除去C 9芳烃 ,并防止C9芳烃在解吸剂输入中积累。 消除了提取塔底部料流的分馏塔,降低了成本,降低了萃余塔的能量需求。

    Zeolitic para-xylene separation with tetralin derivatives as heavy
desorbent
    28.
    发明授权
    Zeolitic para-xylene separation with tetralin derivatives as heavy desorbent 失效
    用四氢萘衍生物作为重解吸剂的沸石对二甲苯分离

    公开(公告)号:US5107062A

    公开(公告)日:1992-04-21

    申请号:US664734

    申请日:1991-03-05

    CPC classification number: C07C7/13

    Abstract: A chromatographic process able to separate paraxylene 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 while maintaining the water content of the adsorbent at about 4.2-6% (LOI). 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 or alkyl derivatives of 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: 可以将对二甲苯与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族阳离子的X或Y沸石吸附剂(例如钡和/或钾)在可交换阳离子位点处接触,同时将吸附剂的水含量保持在约 4.2-6%(LOI)。 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,通过用四氢化萘或四氢化萘的烷基衍生物解吸来回收对二甲苯。 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。

    Separation of coumarone from indene
    29.
    发明授权
    Separation of coumarone from indene 失效
    香豆酮与茚的分离

    公开(公告)号:US4992621A

    公开(公告)日:1991-02-12

    申请号:US412951

    申请日:1989-09-26

    CPC classification number: C07C7/13 C10G25/05

    Abstract: The chromatographic adsorption separation of coumarone from indene-containing coal tar distillate feed mixtures with an alkali metal (Group IA) exchanged X-zeolite and polar materials, e.g., ketones, alcohols or esters as desorbents. Also disclosed is a process for separating a coumarone-indene coextract with sodium-exchanged Y zeolite and toluene as desorbent.

    Abstract translation: 来自含茚煤焦油馏出物进料混合物的苯并呋喃与碱金属(IA组)的交换X沸石和极性物质如酮,醇或酯作为解吸剂进行色谱吸附分离。 还公开了用钠交换的Y沸石和甲苯作为解吸剂分离香豆酮 - 茚共提取物的方法。

    Zeolitic para-ethyltoluene separation with tetralin heavy desorbent
    30.
    发明授权
    Zeolitic para-ethyltoluene separation with tetralin heavy desorbent 失效
    沸石对乙基甲苯与四氢化萘重解吸剂分离

    公开(公告)号:US4956522A

    公开(公告)日:1990-09-11

    申请号:US439058

    申请日:1989-11-20

    CPC classification number: C07C7/13

    Abstract: A chromatographic process able to separate para-ethyltoluene from feed mixtures of C.sub.8 and/or C.sub.9 aromatic hydrocarbons. In the process, the para-ethyltoluene-containing feed mixture is contacted with a Y zeolite adsorbent having potassium at exchangeable cationic sites. The para-ethyltoluene is selectively adsorbed onto the adsorbent. The non-adsorbed components of the feed are then removed from the adsorbent and the para-ethyltoluene recovered by desorption with tetralin or alkyl or dialkyl derivatives of tetralin or alkyl derivatives of naphthalene. The other C.sub.9 's and the xylene isomers in the raffinate and p-ethyltoluene in the extract can be separated from the heavy desorbent by fractionation of the raffinate or extract and the desorbent recycled to the process.

    Abstract translation: 从C8和/或C9芳烃的进料混合物中分离出对 - 乙基甲苯的色谱法。 在此过程中,将含对乙基甲苯的进料混合物与具有可交换阳离子位点钾的Y沸石吸附剂接触。 对乙基甲苯选择性吸附在吸附剂上。 然后从吸附剂中除去进料的未吸附组分,通过用四氢化萘或萘醌的烷基或二烷基衍生物或萘的烷基衍生物解吸而回收的对 - 乙基甲苯。 萃取液中的其余C9和萃余液中的二甲苯异构体和对乙基甲苯可以通过萃取液的分级分离和再循环到该方法中的解吸剂与重质脱附剂分离。

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