-
公开(公告)号：US20150322025A1
公开(公告)日：2015-11-12
申请号：US14806498
申请日：2015-07-22
IPC分类号： C07D301/32
CPC分类号： C07D301/32 , B01J19/245 , B01J2219/24 , C07D301/12 , C07D301/36
摘要： There is provided a process for manipulating the amount of alkyl alcohol in a product stream, e.g., such as an alkylene oxide product stream. More particularly, and in contrast to conventional processes wherein substantially all of the alkyl alcohol must be separated and desirably recycled, in the present process, a greater amount of alkyl alcohol may be allowed to remain in a partially refined alkylene oxide product stream. The residual alkyl alcohol is subsequently substantially entirely reacted to form a downstream product, e.g., a glycol ether, which is more easily separated from the alkylene oxide product stream. Indeed, the amount of alkyl alcohol in the partially refined alkylene oxide product stream can be selected based upon the output of glycol ethers, if desired.
摘要翻译： 提供了一种操纵产物流中烷基醇的量的方法，例如烯化氧产物流。 更具体地，与其中基本上所有烷基醇必须分离并期望再循环的常规方法相反，在本方法中，可以使更多量的烷基醇保留在部分精制的环氧烷产物流中。 残留的烷基醇随后基本上完全反应以形成下游产物，例如乙二醇醚，其更容易从环氧烷产物流中分离出来。 实际上，如果需要，可以基于二醇醚的输出来选择部分精制的环氧烷产物流中的烷基醇的量。
-
公开(公告)号：US20240325985A1
公开(公告)日：2024-10-03
申请号：US18580191
申请日：2022-07-21
发明人： Abhishek Roy , Thomas C. Fitzgibbons , Li Tang , Surendar R. Venna , Derrick W. Flick , Nikki J. Montanez , Hali J. McCurry , James B. Heard , Barry B. Fish
CPC分类号： B01D67/0067 , B01D53/228 , B01D69/02 , B01D69/088 , B01D71/021 , B01D2256/16 , B01D2256/22 , B01D2256/24 , B01D2257/102 , B01D2257/7022 , B01D2323/081 , B01D2323/60 , B01D2325/023
摘要： A method of manufacturing a hollow fiber carbon membrane, the method includes heating a polymeric precursor to a pyrolysis temperature that is greater than or equal to 900° C. and less than or equal to 1200° C., and pyrolyzing the polymeric precursor at the pyrolysis temperature in a pyrolysis atmosphere that comprises oxygen in an amount that is greater than 0 ppm and less than 200 ppm.
-
公开(公告)号：US20160159761A1
公开(公告)日：2016-06-09
申请号：US15043368
申请日：2016-02-12
IPC分类号： C07D301/32 , B01J19/24 , C07D301/12
CPC分类号： C07D301/32 , B01J19/245 , B01J2219/24 , C07D301/12 , C07D301/36
摘要： There is provided a manufacturing assembly for the production of an alkylene oxide and a stream of glycol ethers. The manufacturing assembly produces the alkylene oxide and stream of glycol without the use of equipment for separating substantially all of the alkyl alcohol from the alkylene oxide product stream. Thus, the use of additional pieces of equipment can be avoided, or the equipment required to effectuate any required further separation and/or purification may be smaller and/or cheaper to purchase and/or operate.
摘要翻译： 提供了用于生产环氧烷和二醇醚流的制造组件。 制造组件产生环氧烷和二醇流，而不使用用于从烯化氧产物流中分离基本上所有烷基醇的设备。 因此，可以避免使用额外的设备，或者实现任何所需的进一步分离和/或净化所需的设备可能更小和/或更便宜地购买和/或操作。
-
4.发明授权公开(公告)号：US09643898B2
公开(公告)日：2017-05-09
申请号：US15030634
申请日：2014-11-17
发明人： Derrick W. Flick , Mark W. Stewart
CPC分类号： C07C1/24 , B01J21/04 , B01J29/40 , C07C2521/04 , C07C2529/40 , Y02P20/52 , C07C11/04
摘要： Effect adiabatic, catalytic alkanol (alcohol) dehydration using two or more sequential dehydration catalyst beds each of which has disposed therein a different catalyst and, preferably, eliminating heating and heating apparatus disposed between each sequential pair of dehydration catalyst beds.
-
5.发明申请ALKANOL TO ALKYLENE CONVERSION USING AT LEAST TWO DIFFERENT CATALYSTS IN SEQUENTIAL ORDER 有权使用至少两种不同的催化剂进行碱性转化的烷基转化酶公开(公告)号：US20160244383A1
公开(公告)日：2016-08-25
申请号：US15030634
申请日：2014-11-17
发明人： Derrick W. Flick , Mark W. Stewart
CPC分类号： C07C1/24 , B01J21/04 , B01J29/40 , C07C2521/04 , C07C2529/40 , Y02P20/52 , C07C11/04
摘要： Effect adiabatic, catalytic alkanol (alcohol) dehydration using two or more sequential dehydration catalyst beds each of which has disposed therein a different catalyst and, preferably, eliminating heating and heating apparatus disposed between each sequential pair of dehydration catalyst beds.
摘要翻译： 使用两个或更多个连续的脱水催化剂床进行绝热的催化链烷醇（醇）脱水，每个脱水催化剂床在其中设置有不同的催化剂，优选地消除了设置在每个顺序的一对脱水催化剂床之间的加热和加热装置。
-
公开(公告)号：US09822087B2
公开(公告)日：2017-11-21
申请号：US15043368
申请日：2016-02-12
IPC分类号： B01J19/00 , B01J19/24 , C07D301/00 , C07D301/02 , C07D301/03 , C07D301/32 , C07D301/36 , C07D301/12
CPC分类号： C07D301/32 , B01J19/245 , B01J2219/24 , C07D301/12 , C07D301/36
摘要： There is provided a manufacturing assembly for the production of an alkylene oxide and a stream of glycol ethers. The manufacturing assembly produces the alkylene oxide and stream of glycol without the use of equipment for separating substantially all of the alkyl alcohol from the alkylene oxide product stream. Thus, the use of additional pieces of equipment can be avoided, or the equipment required to effectuate any required further separation and/or purification may be smaller and/or cheaper to purchase and/or operate.
-
公开(公告)号：US09273019B2
公开(公告)日：2016-03-01
申请号：US14806498
申请日：2015-07-22
IPC分类号： C07D301/32
CPC分类号： C07D301/32 , B01J19/245 , B01J2219/24 , C07D301/12 , C07D301/36
摘要： There is provided a process for manipulating the amount of alkyl alcohol in a product stream, e.g., such as an alkylene oxide product stream. More particularly, and in contrast to conventional processes wherein substantially all of the alkyl alcohol must be separated and desirably recycled, in the present process, a greater amount of alkyl alcohol may be allowed to remain in a partially refined alkylene oxide product stream. The residual alkyl alcohol is subsequently substantially entirely reacted to form a downstream product, e.g., a glycol ether, which is more easily separated from the alkylene oxide product stream. Indeed, the amount of alkyl alcohol in the partially refined alkylene oxide product stream can be selected based upon the output of glycol ethers, if desired.
-
-
-
-
-
-
搜索结果
7 条记录 (耗时 0.015 秒)
