Separation of citric acid from gluconic acid in fermentation broth using a weakly or strongly basic anionic exchange resin adsorbent
    51.
    发明授权
    Separation of citric acid from gluconic acid in fermentation broth using a weakly or strongly basic anionic exchange resin adsorbent 有权
    使用弱碱性或强碱性阴离子交换树脂吸附剂在发酵液中分离柠檬酸与葡萄糖酸

    公开(公告)号:US07439392B2

    公开(公告)日:2008-10-21

    申请号:US11757610

    申请日:2007-06-04

    IPC分类号: C07C51/42 C07C59/265

    CPC分类号: C07C51/47 C07C59/265

    摘要: Citric acid is separated from a fermentation broth containing gluconic acid by using an adsorbent comprising a water-insoluble, macroreticular or gel, strongly or weakly basic anionic exchange resin possessing quaternary or tertiary amine functional groups, said a anionic exchange resin having a cross-linked acrylic or styrene resin matrix and a desorbent comprising water or dilute sulfuric acid. The pH of the feed is maintained below the first ionization constant (pKa1) of citric acid to maintain selectivity.

    摘要翻译: 通过使用包含具有季铵或叔胺官能团的不溶于水,大网络或凝胶,强或弱碱性阴离子交换树脂的吸附剂,将柠檬酸与含有葡萄糖酸的发酵液分离,所述阴离子交换树脂具有交联 丙烯酸或苯乙烯树脂基质和包含水或稀硫酸的解吸剂。 饲料的pH值保持在柠檬酸的第一电离常数(pKa 1 H 1/2)以下以保持选择性。

    Process for removal of oxygenates from a paraffin stream
    52.
    发明授权
    Process for removal of oxygenates from a paraffin stream 有权
    从石蜡流中除去含氧化合物的方法

    公开(公告)号:US07368618B2

    公开(公告)日:2008-05-06

    申请号:US11457889

    申请日:2006-07-17

    IPC分类号: C07C5/327

    摘要: The present invention comprises a process for removal of oxygenates from a paraffin-rich or olefin-rich paraffin stream which comprises passing a feed stream, comprising one or more C10 to C15 feed paraffins or C10 to C15 olefin-rich paraffin stream and one or more oxygenates through an adsorbent bed comprising one or more adsorbents selected from silica gel, activated alumina and sodium x zeolites to remove essentially all of said oxygenates; and recovering said paraffins. A second adsorbent bed may be employed to more thoroughly remove these oxygenates.

    摘要翻译: 本发明包括从富含链烷烃或富烯烃的石蜡流中除去含氧化合物的方法,该方法包括将含有一个或多个C 10的进料流送入C 15 通过吸附床将含有一种或多种选自硅胶,活性氧化铝和吸附剂的吸附剂的烷烃或C 10向富含C 15的富烯烃链烷烃流和一种或多种含氧化合物进料, 钠x沸石以除去基本上所有的含氧化合物; 并回收所述石蜡。 可以使用第二吸附剂床来更彻底地除去这些含氧化合物。

    MIXED MATRIX ADSORBENT FOR PARA-XYLENE SEPARATION
    53.
    发明申请
    MIXED MATRIX ADSORBENT FOR PARA-XYLENE SEPARATION 有权
    用于PARA-XYLENE分离的混合基质吸附剂

    公开(公告)号:US20080076952A1

    公开(公告)日:2008-03-27

    申请号:US11534264

    申请日:2006-09-22

    IPC分类号: C07C7/12

    CPC分类号: C07C7/13 C07C15/08

    摘要: A process for separating C8 aromatics is disclosed. The process uses at least two adsorbents, and in particular a BaX zeolite and a KY zeolite, for the separation of para-xylene from a mixture of C8 aromatics.

    摘要翻译: 公开了一种用于分离C8芳族化合物的方法。 该方法使用至少两种吸附剂,特别是BaX沸石和KY沸石,用于从C8芳族化合物的混合物中分离对二甲苯。

    Adsorptive removal of carbonyl impurities from oxygenated organic liquids
    54.
    发明授权
    Adsorptive removal of carbonyl impurities from oxygenated organic liquids 失效
    从含氧有机液体中吸附去除羰基杂质

    公开(公告)号:US06346645B1

    公开(公告)日:2002-02-12

    申请号:US09551642

    申请日:2000-04-18

    IPC分类号: C07C5112

    CPC分类号: C07C51/12 C07C51/48 C07C53/08

    摘要: Carbonyl compounds (e.g. acetone and acetaldehyde) are often present as impurities in oxygenated organic liquids such as acetic acid made by the carbonylation of methanol or in phenol produced by the oxidation of cumene. These impurities can render petrochemical products unsuitable for long-term storage or otherwise adversely affect downstream processing operations. It has now been found that detrimental carbonyl impurities can be easily removed from oxygenated organic liquids by contact with resins having amine functional groups.

    摘要翻译: 羰基化合物(例如丙酮和乙醛)通常作为杂质存在于氧化的有机液体中,例如通过羰基化甲醇或通过异丙苯的氧化产生的苯酚制得的乙酸。 这些杂质可能导致石化产品不适合长期储存或以其他方式不利地影响下游加工操作。 现在已经发现,通过与具有胺官能团的树脂接触,可以容易地从有氧氧化有机液体中除去有害的羰基杂质。

    Process for regenerating an adsorbent
    55.
    发明授权
    Process for regenerating an adsorbent 失效
    再生吸附剂的方法

    公开(公告)号:US06342462B1

    公开(公告)日:2002-01-29

    申请号:US09274005

    申请日:1999-03-22

    IPC分类号: B01J3864

    摘要: A novel process for the regeneration of a solid adsorbent which is at least partially spent and has a reactive metal (e.g. silver) dispersed thereon is disclosed. The regeneration consists of a step whereby accumulated metal-containing reaction products formed during adsorptive service are removed by stripping the spent or partially spent adsorbent with a suitable stripping solution such as sodium thiosulfate. After detrimental metal-containing deposits are stripped, the adsorbent is then subjected to a reactivation step in which the regenerated adsorbent is contacted with a solution containing a reactive metal compound (e.g. silver nitrate). Reactivating the adsorbent therefore adds an incremental amount of the reactive metal onto the adsorbent. Regeneration of the adsorbent according to the two-step method of the present invention thus effectively prolongs its useful life. The present invention is particularly applicable to adsorbents used in processes involving the adsorption of iodine-containing compounds from contaminated feed streams.

    摘要翻译: 公开了一种用于再生固体吸附剂的新方法,其至少部分地被消耗并且具有分散在其上的反应性金属(例如银)。 再生包括通过用合适的汽提溶液例如硫代硫酸钠汽提废弃或部分用过的吸附剂来除去吸附剂中形成的含金属反应产物的步骤。 在除去有害的含金属沉积物之后,然后对吸附剂进行再活化步骤,其中再生的吸附剂与含有反应性金属化合物(例如硝酸银)的溶液接触。 因此,重新激活吸附剂会增加一定量的反应性金属到吸附剂上。 因此,根据本发明的两步法的吸附剂的再生有效地延长了其使用寿命。 本发明特别适用于涉及从受污染的进料流吸附含碘化合物的方法中使用的吸附剂。

    Carbonylation process with integrated heat exchange
    56.
    发明授权
    Carbonylation process with integrated heat exchange 失效
    具有集成热交换的羰基化过程

    公开(公告)号:US6114576A

    公开(公告)日:2000-09-05

    申请号:US215734

    申请日:1998-12-18

    CPC分类号: C07C51/12

    摘要: A process for the production of a carboxylic acid in the presence of solid catalyst particles that uses the exothermic heat of reaction with high efficiency in recovering the carboxylic acid product is disclosed. This process uses indirect heat exchange to transfer the heat of reaction to another stream, without the need for an additional heat transfer fluid such as steam. This invention is especially applicable to the production of acetic acid.

    摘要翻译: 公开了一种在固体催化剂颗粒存在下生产羧酸的方法,该方法使用反应的放热热回收羧酸产物,其效率高。 该方法使用间接热交换将反应热转移到另一种流,而不需要额外的传热流体,例如蒸汽。 本发明特别适用于生产乙酸。

    Single vessel distillation and adsorption apparatus
    57.
    发明授权
    Single vessel distillation and adsorption apparatus 失效
    单容器蒸馏和吸附装置

    公开(公告)号:US5565066A

    公开(公告)日:1996-10-15

    申请号:US319919

    申请日:1994-10-07

    IPC分类号: B01D3/14 B01D3/00 B01D15/00

    CPC分类号: B01D3/14 Y10S203/06

    摘要: The present invention is a single vessel apparatus for separating at least a first component from a second component of a process stream. The apparatus has a vertically-elongated vessel which contains a plurality of vertically spaced apart distillation contactors for vapor and liquid distillation and an adsorbent-retaining volume defined at least in part by a solids-impermeable member located above the contactors for passing a fluid into the retaining volume. The apparatus also contains a mechanism for adding adsorbent above the solids-impermeable member and a mechanism for withdrawing adsorbent particles from the retaining volume to contact the fluid with adsorbent particles and to provide at least intermittent downward gravity flow of adsorbent particles through the retaining volume and to selectively adsorb a portion of the fluid. The apparatus further contains a regenerator for desorbing fluids from adsorbent particles which is in communication with the mechanism for adding adsorbent above the solids-impermeable member and the means for withdrawing adsorbent particles from the adsorbent-retaining volume. The fluids are desorbed in the regenerator by passing a regenerant into and collecting the regenerant from the regenerator. Finally, the apparatus also contains a mechanism for adding fluid to and withdrawing fluid from the vessel. The benefit of the invention is a high purity single vessel separation unit at reduced capital equipment costs.

    摘要翻译: 本发明是用于从至少第一组分与工艺流的第二组分分离的单容器装置。 该装置具有垂直细长的容器,其包含用于蒸气和液体蒸馏的多个垂直间隔开的蒸馏接触器,以及至少部分地由位于接触器上方的固体不可渗透构件限定的吸附剂保留体积,用于将流体传入 保持体积。 该装置还包含用于在固体不可渗透构件上添加吸附剂的机构,以及用于从保留体积中吸出吸附剂颗粒以吸附流体与吸附剂颗粒接触并提供吸附剂颗粒至少间断向下重力流过保持体积的机构, 以选择性地吸附流体的一部分。 该设备还包含用于从吸附剂颗粒解吸流体的再生器,其与用于在固体不可渗透构件上添加吸附剂的机构连接,以及用于从吸附剂保持体积中抽出吸附剂颗粒的装置。 通过使再生剂进入再生器并从再生器收集再生剂,在再生器中解吸流体。 最后,该装置还包含用于向容器中加入流体和从容器中取出流体的机构。 本发明的优点是在降低资本设备成本的情况下是高纯度单容器分离单元。

    Preparation of a heat-stable lactic acid
    58.
    发明授权
    Preparation of a heat-stable lactic acid 失效
    制备热稳定性乳酸

    公开(公告)号:US5488156A

    公开(公告)日:1996-01-30

    申请号:US363662

    申请日:1994-12-23

    IPC分类号: C07C51/42 C07C51/487 C12P7/56

    CPC分类号: C12P7/56 C07C51/42 C07C51/487

    摘要: Lactic acid formed via fermentation generally is susceptible to the development of color bodies when heated to temperatures of approximately 180.degree. C. and above. Color development appears to result from carbonization of small amounts of carbohydrates. Consequently a heat-stable lactic acid may be produced by subjecting an aqueous solution of lactic acid to temperatures between about 180 and 230.degree. C. for a time sufficient to carbonize the carbohydrates, with subsequent removal of the color bodies using standard decolorants such as activated charcoal. Heat treatment may be applied either directly to the broth or to an aqueous solution resulting from one or more processing steps applied to the fermentation broth.

    摘要翻译: 通过发酵形成的乳酸通常在加热至约180℃及以上的温度时容易发色。 颜色发展似乎是由于少量碳水化合物的碳化所致。 因此,可以通过使乳酸水溶液在约180℃和230℃之间的温度下进行足以碳化碳水化合物的时间,然后用标准的脱色剂如活化的 木炭。 热处理可以直接施用到肉汤或由应用于发酵液的一个或多个加工步骤产生的水溶液。

    Process for the adsorptive separation of metaxylene from aromatic
hydrocarbons
    59.
    发明授权
    Process for the adsorptive separation of metaxylene from aromatic hydrocarbons 失效
    来自芳烃的间二甲苯的吸附分离方法

    公开(公告)号:US5382747A

    公开(公告)日:1995-01-17

    申请号:US110528

    申请日:1993-08-23

    IPC分类号: C07C7/12 C07C7/13 C07C15/08

    CPC分类号: C07C7/13

    摘要: Metaxylene is recovered from a mixture of C.sub.8 aromatic hydrocarbons including other xylenes by liquid phase adsorptive separation using a sodium or sodium and lithium exchanged Y zeolite as the adsorbent. Performance is improved by maintaining the adsorbent in a narrow range of temperature and hydration. Toluene is the preferred desorbent.

    摘要翻译: 通过使用钠或钠和锂交换的Y沸石作为吸附剂通过液相吸附分离从包括其它二甲苯的C8芳族烃的混合物中回收亚甲硅氧烷。 通过将吸附剂保持在窄的温度和水合范围内来提高性能。 甲苯是优选的脱附剂。

    Process for separating triglycerides having different degrees of
unsaturation
    60.
    发明授权
    Process for separating triglycerides having different degrees of unsaturation 失效
    用于分离具有不同不饱和度的甘油三酸酯的方法

    公开(公告)号:US5175324A

    公开(公告)日:1992-12-29

    申请号:US687644

    申请日:1991-04-19

    IPC分类号: C11B7/00

    CPC分类号: C11B7/0083 C11B7/0008

    摘要: The separation of monounsaturated triglycerides from polyunsaturated triglycerides is achieved by an adsorptive chromatographic process in liquid phase with silica gel as the adsorbent at temperatures higher than about 100.degree. C. Desorbents in the separation process include ketones, having from 3 to 8 carbon atoms in concentrations of up to about 25% (vol.) in normal or branched alkanes, e.g., n-hexane or iso-octane, or p-cymene in concentrations of 20% (vol.) to 100%.

    摘要翻译: 通过在高于约100℃的温度下通过硅胶作为吸附剂的液相中的吸附色谱法来实现多不饱和甘油三酸酯的单不饱和甘油三酯的分离。分离过程中的脱附剂包括具有3至8个碳原子浓度的酮 在正己烷或异辛烷或浓度为20%(体积)至100%的对甲基异丙基苯的正链或支链烷烃中的含量高达约25%(体积)。