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    Process for the production of anhydrides
    2.
    发明授权
    Process for the production of anhydrides 有权
    酸酐生产工艺

    公开(公告)号：US08937190B2

    公开(公告)日：2015-01-20

    申请号：US13580108

    申请日：2012-02-03

    Applicant: Simon Nicholas Tilley

    Inventor： Simon Nicholas Tilley

    IPC: C07D307/34 ,  C07C65/00 ,  C07C51/54 ,  B01J8/02 ,  B01J8/06 ,  B01J19/24 ,  C07D307/60 ,  B01J23/22 ,  B01J27/198

    CPC classification number: C07C51/54 ,  B01J8/0285 ,  B01J8/067 ,  B01J19/2485 ,  B01J23/22 ,  B01J27/198 ,  B01J35/04 ,  B01J2208/00814 ,  C07D307/60

    Abstract: In a process for producing anhydrides in a tubular reactor, gaseous reactants are passed downwardly through at least one reactor tube to a catalyst carrier where they pass into a passage defined by an inner perforated wall of a catalyst container before passing radially through the catalyst bed towards a perforated outer container wall. The reaction occurs as gas contacts the catalyst. Unreacted reactant and product exits the container though the perforated outer wall and then upwardly between an inner surface of a container skirt and the outer wall of the container and then over the end of the skirt and caused to flow downwardly between the outer surface of the skirt and the inner surface of the reactor tube where heat transfer takes place. These steps are repeated at any subsequent catalyst carrier product is then removed from the reactor outlet.

    Abstract translation: 在管式反应器中生产酸酐的方法中，气态反应物通过至少一个反应器管道向下通过催化剂载体，在催化剂载体中，其通过催化剂容器的内部穿孔壁限定的通道中，然后通过催化剂床径向通过催化剂床 穿孔外容器壁。 反应随着气体与催化剂接触而发生。 未反应的反应物和产物通过穿孔的外壁离开容器，然后在容器裙部的内表面和容器的外壁之间向上离开容器，然后超过裙部的端部并且在裙部的外表面之间向下流动 以及发生热传递的反应管的内表面。 在随后的任何催化剂载体产物随后从反应器出口移出时重复这些步骤。

    Process For Producing Fatty Alcohols From Fatty Acids
    3.
    发明申请
    Process For Producing Fatty Alcohols From Fatty Acids 有权
    从脂肪酸生产脂肪醇的方法

    公开(公告)号：US20140323773A1

    公开(公告)日：2014-10-30

    申请号：US13884815

    申请日：2012-11-01

    Applicant: Davy Process Technology Limited

    Inventor： Paul Appleton ,  Michael Anthony Wood ,  Robert Wild

    IPC: C07C29/128

    CPC classification number: C07C29/1285 ,  C07C29/128 ,  C07C29/149 ,  C07C31/125 ,  C07C67/03 ,  C07C67/08 ,  C07C69/26 ,  C07C69/24

    Abstract: In a process for the production of fatty alcohol(s) a fatty acid or fatty acid mixture is subjected to esterification with a lower alkanol to form a stream comprising the corresponding lower alkyl ester or esters. The stream is vaporised and subjected to hydrogenation to form a stream comprising fatty alcohol(s) and an amount of unconverted lower alkyl ester(s). This stream is subjected to transesterification in a wax ester reactor in the presence of a solid transesterification catalyst. Fatty alcohol(s) and wax ester(s) are then separated by distillation to yield a fatty alcohol(s) product and a stream comprising wax ester(s). The stream of wax ester(s) is passed to a second hydrogenation zone to effect hydrogenation in the liquid phase to revert the wax ester(s) to fatty alcohol(s), which are returned to the distillation separation step.

    Abstract translation: 在生产脂肪醇的方法中，脂肪酸或脂肪酸混合物用低级烷醇进行酯化以形成包含相应的低级烷基酯或酯的料流。 将该物流汽化并进行氢化以形成包含脂肪醇和一定量的未转化的低级烷基酯的物流。 在固体酯交换催化剂存在下，将该料流在蜡酯反应器中进行酯交换。 然后通过蒸馏分离脂肪醇和蜡酯，得到脂肪醇产物和包含蜡酯的物流。 将蜡酯流送入第二氢化区以在液相中进行氢化以将蜡酯还原成脂肪醇，将其返回至蒸馏分离步骤。

    Reactor
    5.
    发明申请
    Reactor 有权
    反应堆

    公开(公告)号：US20140024863A1

    公开(公告)日：2014-01-23

    申请号：US13583335

    申请日：2012-01-12

    Applicant: Edward Adrian Lord ,  Arthur James Reason

    Inventor： Edward Adrian Lord ,  Arthur James Reason

    IPC: B01J19/24 ,  C07C29/141

    CPC classification number: B01J19/248 ,  B01J8/0465 ,  B01J2208/00265 ,  B01J2219/00024 ,  C07C7/163 ,  C07C29/141 ,  C10G2/32 ,  C10G3/42 ,  C10G45/32 ,  C10G45/44 ,  C10G49/002 ,  C10G2300/1096 ,  C10G2300/4081 ,  Y02P20/584 ,  Y02P30/20 ,  Y10S585/903 ,  C07C11/08 ,  C07C31/125

    Abstract: A liquid/gas reactor includes a bulk catalyst bed and means for supplying fresh feed and recycled at least partially converted liquid product stream to the bulk catalyst bed. The reactor also includes means for collecting an at least partially converted liquid product stream from the bulk catalyst bed and recycling at least a portion thereto. A minor catalyst bed extends substantially vertically through the bulk catalyst bed. Means for supplying recycled at least partially converted product stream only to the minor catalyst bed is also provided. A separating wall is disposed between the bulk catalyst bed and the minor catalyst bed.

    Abstract translation: 液体/气体反应器包括主体催化剂床和用于将新鲜进料和再循环的至少部分转化的液体产物流供应到本体催化剂床的装置。 反应器还包括用于收集来自大量催化剂床的至少部分转化的液体产物流并将至少一部分再循环的装置。 较小的催化剂床基本垂直延伸穿过整体催化剂床。 还提供了用于将再循环的至少部分转化的产物流仅供应到次要催化剂床的装置。 分离壁设置在主体催化剂床和次催化剂床之间。

    Process and System For The Separation And Drying of Carboxylic Acid Crystals
    6.
    发明申请
    Process and System For The Separation And Drying of Carboxylic Acid Crystals 有权
    分离和干燥羧酸晶体的方法和系统

    公开(公告)号：US20130245317A1

    公开(公告)日：2013-09-19

    申请号：US13698732

    申请日：2011-05-18

    Applicant: Julian Stuart Gray ,  Michael William Winter ,  Andrea Gnagnetti

    Inventor： Julian Stuart Gray ,  Michael William Winter ,  Andrea Gnagnetti

    IPC: C07C51/47

    CPC classification number: C07C51/47 ,  C07C51/43 ,  C07C63/26 ,  C07C63/24

    Abstract: In a process for the separation and drying of crude carboxylic acid crystals from a slurry in a solvent, the slurry is supplied to a filter operating at pressure and at a temperature above the atmospheric boiling point of the solvent. A cake of separated crystals is removed from the filter and passed to a thermal dryer. In a system for the separation and drying of crude carboxylic acid from a slurry in a solvent, a pressure filter device has a slurry inlet and an outlet for a cake of carboxylic acid crystals. The system also has a thermal dryer and means for transporting the cake of carboxylic acid crystals from the pressure filter device to the dryer. The pressure filter device is configured to operate at a pressure and temperature above the atmospheric boiling point of the solvent.

    Abstract translation: 在从溶剂中的浆料中分离和干燥粗羧酸晶体的方法中，将浆料供给到在压力和高于溶剂的常压沸点的温度下操作的过滤器。 将分离的晶体的滤饼从过滤器中取出并送入热干燥器。 在用于从溶剂中的浆料中分离和干燥粗羧酸的系统中，压力过滤装置具有浆料入口和羧酸晶体饼的出口。 该系统还具有热干燥器和用于将羧酸晶体块从压力过滤装置输送到干燥器的装置。 压力过滤装置构造成在高于溶剂的大气沸点的压力和温度下操作。

    PROCESS FOR THE PRODUCTION OF SUBSTITUTE NATURAL GAS
    7.
    发明申请
    PROCESS FOR THE PRODUCTION OF SUBSTITUTE NATURAL GAS 有权
    生产替代天然气的过程

    公开(公告)号：US20130210938A1

    公开(公告)日：2013-08-15

    申请号：US13805940

    申请日：2011-06-27

    Applicant: Philip Henry Donald Eastland ,  Jonathan Geoffrey Gavin ,  David Andrew Walker

    Inventor： Philip Henry Donald Eastland ,  Jonathan Geoffrey Gavin ,  David Andrew Walker

    IPC: C10L3/08

    CPC classification number: C10L3/08

    Abstract: In a process for the production of substitute natural gas, a feed gas is provided to a first and/or second and/or subsequent bulk methanator. The feed gas is subjected to methanation in the presence of a suitable catalyst. An at least partially reacted stream from the first bulk methanator is removed and supplied to the second and/or subsequent bulk methanator where it is subjected to further methanation. A product stream from the final bulk methanator is passed to a trim methanator train where it is subjected to further methanation. A recycle stream is removed downstream of the first, second or subsequent bulk methanator, and, in any order, passed through a compressor, subjected to cooling and then supplied to a trim and/or recycle methanator for further methanation before being recycled to the first and/or second and/or subsequent methanator.

    Abstract translation: 在生产替代天然气的方法中，将进料气体提供给第一和/或第二和/或随后的主体甲烷化器。 进料气体在合适的催化剂存在下进行甲烷化。 去除来自第一批量甲烷化器的至少部分反应的物流并将其供应到第二和/或随后的主体甲烷化器中，在那里进行甲烷化。 来自最终的大量甲烷化器的产物流被送到修剪甲烷化器列，在那里进行进一步甲烷化。 在第一，第二或随后的主体甲烷化器的下游除去再循环流，并以任何顺序通过压缩机，进行冷却，然后供给到装饰和/或再循环甲烷化器中进一步甲烷化，然后再循环至第一 和/或第二和/或其后的甲烷化器。

    Process And System For The Separation Of Carboxylic Acids From A Slurry
    8.
    发明申请
    Process And System For The Separation Of Carboxylic Acids From A Slurry 审中-公开
    从浆液中分离羧酸的方法和系统

    公开(公告)号：US20130190530A1

    公开(公告)日：2013-07-25

    申请号：US13700698

    申请日：2011-06-22

    Applicant: Julian Stuart Gray ,  Michael William Winter ,  Andrea Gnagnetti

    Inventor： Julian Stuart Gray ,  Michael William Winter ,  Andrea Gnagnetti

    IPC: C07C51/42 ,  B01D33/58

    CPC classification number: C07C51/42 ,  B01D33/58 ,  C07C51/43 ,  C07C63/24 ,  C07C63/26

    Abstract: In a process for the separation of carboxylic acid from a slurry in a solvent, a slurry with crystals of carboxylic acid is supplied to a filter operating at pressure and at a temperature above the atmospheric boiling point of the solvent. Inert gas is mixed with the solvent and the mixture is supplied to the filter. A cake of separated crystals is removed from the filter. Inert gas removed from the filter is not recycled. In a system for performing such separation, a pressure filter device has a slurry inlet, and an outlet. Means for mixing inert gas and solvent, and means for supplying the mixture to the pressure filter are provided. The pressure filter device is configured to operate at pressure and at a temperature above the atmospheric boiling point of the solvent. The system does not include means for recycling inert gas removed from the filter.

    Abstract translation: 在将羧酸从溶剂中的浆料中分离的方法中，将具有羧酸结晶的浆料供给到在高于溶剂的常压沸点的压力和温度下操作的过滤器。 将惰性气体与溶剂混合，将混合物供入过滤器。 分离的晶体的滤饼从过滤器中除去。 从过滤器中除去的惰性气体不能回收利用。 在用于进行这种分离的系统中，压力过滤装置具有浆料入口和出口。 提供用于混合惰性气体和溶剂的方法，以及用于将混合物供给到压力过滤器的装置。 压力过滤装置构造成在高于溶剂的常压沸点的压力和温度下操作。 该系统不包括用于回收从过滤器去除的惰性气体的装置。

    Process and plant
    9.
    发明授权
    Process and plant 有权
    工艺和植物

    公开(公告)号：US08101142B2

    公开(公告)日：2012-01-24

    申请号：US10158752

    申请日：2002-05-30

    Applicant: Philip Henry Donald Eastland

    Inventor： Philip Henry Donald Eastland

    IPC: B01J8/04 ,  C07C27/00

    CPC classification number: C12C11/02 ,  B01J8/0407 ,  B01J8/043 ,  B01J8/0442 ,  B01J8/0449 ,  B01J8/0488 ,  C07C29/152 ,  C07C31/04

    Abstract: A reactor system, plant and a process for the production of methanol from synthesis gas is described in which the reactor system comprises: (a) a first reactor adapted to be maintained under methanol synthesis conditions having inlet means for supply of synthesis gas and outlet means for recovery of a first methanol-containing stream, said first reactor being charged with a first volume of a methanol synthesis catalyst through which the synthesis gas flows and on which in use, partial conversion of the synthesis gas to a product gas mixture comprising methanol and un-reacted synthesis gas will occur adiabatically; and (b) a second reactor adapted to be maintained under methanol synthesis conditions having inlet means for supply of the gaseous first methanol-containing stream, outlet means for recovery of a second methanol-containing stream and cooling means, said second reactor being charged with a second volume of a methanol synthesis catalyst through which the gaseous first methanol-containing stream flows and on which, in use, further conversion of the synthesis gas to a product gas mixture comprising methanol will occur.

    Abstract translation: 描述了一种用于从合成气生产甲醇的反应器系统，设备和方法，其中反应器系统包括：（a）适于在甲醇合成条件下保持的第一反应器，其具有用于供应合成气和出口装置的入口装置 用于回收第一含甲醇的物流，所述第一反应器装有第一体积的合成气体流过甲醇合成催化剂，在使用中，合成气部分转化成包含甲醇的产物气体混合物， 未反应的合成气将绝热发生; 和（b）适于在甲醇合成条件下保持的第二反应器，其具有用于供应气体的第一含甲醇流的入口装置，用于回收第二含甲醇流和冷却装置的出口装置，所述第二反应器装有 第二体积的甲醇合成催化剂，气态第一含甲醇流通过该催化剂流动，并且在使用中将进一步将合成气转化为包含甲醇的产物气体混合物。

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