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1. 发明授权

US07378559B2 Continuous process and system of producing polyether polyols 失效
标题翻译：生产聚醚多元醇的连续工艺和体系
公开(公告)号：US07378559B2
公开(公告)日：2008-05-27
申请号：US10545661
申请日：2004-03-05
申请人： Jan W. Verwijs , John W. Weston , Walter J. S. Papadopulos , Richard J. Elwell , Carlos M. Villa
发明人： Jan W. Verwijs , John W. Weston , Walter J. S. Papadopulos , Richard J. Elwell , Carlos M. Villa
IPC分类号： C07C43/11 , C07C43/00
CPC分类号： B01J19/1837 , C08G65/2663 , C08G65/2696
摘要： A continuous process and system for producing polyether polyols that allows for continuously adding an unreacted oxide to a loop reactor while adding at least one thermally deactivating catalyst capable of thermally deactivating prior to decomposition of polyether polyol which can allow for greater concentrations of unreacted oxides and/or a rate of reaction in the loop reactor is at a rate at least two times faster than a rate of reaction in a loop reactor containing less than 14 weight percent unreacted oxide. In a preferred embodiment, the catalyst is a double metal cyanide catalyst and a plug flow reactor is formed in series with the loop reactor wherein neither reactor contains a vapor space.
摘要翻译：一种用于生产聚醚多元醇的连续方法和系统，其允许在环状反应器中连续加入未反应的氧化物，同时加入至少一种能够在聚醚多元醇分解之前热失活的热失活催化剂，其可以允许更大浓度的未反应的氧化物和/ 或者环管反应器中的反应速率比含有少于14重量％未反应氧化物的环管反应器中的反应速度快至少两倍。在优选的实施方案中，催化剂是双金属氰化物催化剂，并且活塞流反应器与环管反应器串联形成，其中两个反应器都不包含蒸气空间。

2. 发明申请

US20080221281A1 CONTINUOUS PROCESS AND SYSTEM OF PRODUCING POLYETHER POLYOLS 审中-公开
标题翻译：连续生产聚醚多元醇的方法和系统
公开(公告)号：US20080221281A1
公开(公告)日：2008-09-11
申请号：US12054782
申请日：2008-03-25
申请人： Jan W. Verwijs , Walter J. S. Papadopulos , John W. Weston , Richard J. Elwell , Carlos M. Villa
发明人： Jan W. Verwijs , Walter J. S. Papadopulos , John W. Weston , Richard J. Elwell , Carlos M. Villa
IPC分类号： C08F2/01
CPC分类号： B01J19/1837 , C08G65/2663 , C08G65/2696
摘要： A continuous process and system for producing polyether polyols that allows for continuously adding an unreacted oxide to a loop reactor while adding at least one thermally deactivating catalyst capable of thermally deactivating prior to decomposition of polyether polyol which can allow for greater concentrations of unreacted oxides and/or a rate of reaction in the loop reactor is at a rate at least two times faster than a rate of reaction in a loop reactor containing less than 14 weight percent unreacted oxide. In a preferred embodiment, the catalyst is a double metal cyanide catalyst and a plug flow reactor is formed in series with the loop reactor wherein neither reactor contains a vapor space.
摘要翻译：一种用于生产聚醚多元醇的连续方法和系统，其允许在环状反应器中连续加入未反应的氧化物，同时加入至少一种能够在聚醚多元醇分解之前热失活的热失活催化剂，其可以允许更大浓度的未反应的氧化物和/ 或者环管反应器中的反应速率比含有少于14重量％未反应氧化物的环管反应器中的反应速度快至少两倍。在优选的实施方案中，催化剂是双金属氰化物催化剂，并且活塞流反应器与环管反应器串联形成，其中两个反应器都不包含蒸气空间。

3. 发明授权

US08912364B2 Continuous loop flow process for polyether polyol production 有权
标题翻译：聚醚多元醇生产的连续循环流程
公开(公告)号：US08912364B2
公开(公告)日：2014-12-16
申请号：US12992025
申请日：2009-05-19
申请人： Carlos M. Villa , John W. Weston , Pradeep Jain , Leigh H. Thompson , Jean-Paul Masy
发明人： Carlos M. Villa , John W. Weston , Pradeep Jain , Leigh H. Thompson , Jean-Paul Masy
IPC分类号： C08G65/00 , C08G65/26
CPC分类号： C08G65/2663 , C08G65/2609 , C08G65/2696 , Y02P20/124
摘要： The present disclosure relates, according to some embodiments, to compositions, apparatus, methods, and systems that may be used to produce polyols, for example, polyether polyols with a narrow range of molecular weights, with little if any unsaturated byproducts, in a sustained and/or continuous reaction, with efficient heat transfer, and/or at high production rates. For example, in some embodiments, teachings of the disclosure may be used to produce polyether polyols in a continuous loop flow process. A continuous loop flow process may be practiced such that heat is effectively transferred and/or product properties (e.g., range of molecular weights) are controllable. For example, a continuous loop flow process may use one or more continuous flow loops comprising a heat exchanger, a means to move material around each loop, inlets for catalyst, monomer, initiator or starter, and an outlet for polyol product.
摘要翻译：根据一些实施方案，本公开涉及可用于制备多元醇的组合物，装置，方法和系统，例如具有窄范围分子量的聚醚多元醇，几乎没有不饱和副产物，在持续的和/或连续反应，有效的热传递和/或以高生产率。例如，在一些实施方案中，本公开的教导可用于在连续环流过程中制备聚醚多元醇。可以实践连续环流过程，使得有效地转移热量和/或产物性质（例如，分子量范围）是可控的。例如，连续环流过程可以使用一个或多个连续流动回路，其包括热交换器，用于在每个回路周围移动材料的装置，用于催化剂，单体，引发剂或起动器的入口以及多元醇产物的出口。

4. 发明授权

US09637593B2 Single column stripping and drying process 有权
公开(公告)号：US09637593B2
公开(公告)日：2017-05-02
申请号：US15046357
申请日：2016-02-17
申请人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
发明人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
IPC分类号： F26B3/00 , C08G65/30 , B01D3/14 , B01D3/26 , B01D3/34 , B01D3/38
CPC分类号： C08G65/30 , B01D3/143 , B01D3/26 , B01D3/343 , B01D3/38
摘要： Organic materials are stripped and dried in a single column having two contact zones. A stripping gas is introduced into an upper contact zone and flows through the organic material in that zone. A drying gas is introduced into a lower contact zone. The drying gas contacts the organic material in both the upper and lower contact zones, and is removed from the top of the column together with the stripping gas. This process permits very efficiently removal of volatile organic compounds as well as efficient drying, while requiring on low levels of the stripping and drying gasses.

5. 发明授权

US09074044B2 Method for continuously producing low equivalent weight polyols using double metal cyanide catalysts 有权
标题翻译：使用双金属氰化物催化剂连续生产低当量多元醇的方法
公开(公告)号：US09074044B2
公开(公告)日：2015-07-07
申请号：US13514372
申请日：2010-12-06
申请人： John W. Weston , Carlos M. Villa , Jean-Paul Masy , Kevin C. Seavey
发明人： John W. Weston , Carlos M. Villa , Jean-Paul Masy , Kevin C. Seavey
IPC分类号： C07C41/03 , C08G65/26
CPC分类号： C08G65/2663 , C08G65/2609 , C08G65/2696
摘要： Polyether polyols having equivalent weights of up to 500 are continuously prepared in the presence of a double metal cyanide catalyst. A first step of the reaction is performed at a temperature of at least 150° C., while controlling the hydroxyl content and unreacted alkylene oxide content of the reaction mixture to within certain ranges. A portion of that reaction mixture is withdrawn and permitted to react non-isothermally to consume the unreacted alkylene oxide. This process is highly efficient, does not result in catalyst deactivation, as is commonly seen in previous processes, and does not produce a significant ultra high molecular weight tail.
摘要翻译：在双金属氰化物催化剂存在下，连续制备具有多达500当量重量的聚醚多元醇。反应的第一步在至少150℃的温度下进行，同时将反应混合物的羟基含量和未反应的烯化氧含量控制在一定范围内。将该反应混合物的一部分取出并允许非等温反应以消耗未反应的环氧烷。该方法是高效的，不会导致催化剂失活，如在之前的方法中通常所见，并且不产生显着的超高分子量尾。

6. 发明申请

US20120279082A1 Single Column Stripping and Drying Process 审中-公开
标题翻译：单柱剥离和干燥过程
公开(公告)号：US20120279082A1
公开(公告)日：2012-11-08
申请号：US13497267
申请日：2010-09-21
申请人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
发明人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
IPC分类号： F26B7/00
CPC分类号： C08G65/30 , B01D3/143 , B01D3/26 , B01D3/343 , B01D3/38
摘要： Organic materials are stripped and dried in a single column having two contact zones. A stripping gas is introduced into an upper contact zone and flows through the organic material in that zone. A drying gas is introduced into a lower contact zone. The drying gas contacts the organic material in both the upper and lower contact zones, and is removed from the top of the column together with the stripping gas. This process permits very efficiently removal of volatile organic compounds as well as efficient drying, while requiring on low levels of the stripping and drying gasses.
摘要翻译：将有机材料剥离并在具有两个接触区的单个柱中干燥。汽提气体被引入上部接触区域并流过该区域中的有机材料。干燥气体被引入下接触区域。干燥气体与上接触区域和下接触区域中的有机材料接触，并与汽提气体一起从柱顶部除去。该方法允许非常有效地除去挥发性有机化合物以及有效的干燥，同时需要低水平的汽提和干燥气体。

7. 发明申请

US20120283483A1 METHOD FOR CONTINUOUSLY PRODUCING LOW EQUIVALENT WEIGHT POLYOLS USING DOUBLE METAL CYANIDE CATALYSTS 有权
标题翻译：使用双金属氰化物催化剂连续生产低等效重量聚合物的方法
公开(公告)号：US20120283483A1
公开(公告)日：2012-11-08
申请号：US13514372
申请日：2010-12-06
申请人： John W. Weston , Carlos M. Villa , Jean-Paul Masy , Kevin C. Seavey
发明人： John W. Weston , Carlos M. Villa , Jean-Paul Masy , Kevin C. Seavey
IPC分类号： C08G65/10
CPC分类号： C08G65/2663 , C08G65/2609 , C08G65/2696
摘要： Polyether polyols having equivalent weights of up to 500 are continuously prepared in the presence of a double metal cyanide catalyst. A first step of the reaction is performed at a temperature of at least 1500 C, while controlling the hydroxyl content and unreacted alkylene oxide content of the reaction mixture to within certain ranges. A portion of that reaction mixture is withdrawn and permitted to react non-isothermally to consume the unreacted alkylene oxide. This process is highly efficient, does not result in catalyst deactivation, as is commonly seen in previous processes, and does not produce a significant ultra high molecular weight tail.
摘要翻译：在双金属氰化物催化剂存在下，连续制备具有多达500当量重量的聚醚多元醇。在至少1500℃的温度下进行反应的第一步，同时将反应混合物的羟基含量和未反应的烯化氧含量控制在一定范围内。将该反应混合物的一部分取出并允许非等温反应以消耗未反应的环氧烷。该方法是高效的，不会导致催化剂失活，如在之前的方法中通常所见，并且不产生显着的超高分子量尾。

8. 发明申请

US20160159978A1 SINGLE COLUMN STRIPPING AND DRYING PROCESS 有权
标题翻译：单列剥离和干燥过程
公开(公告)号：US20160159978A1
公开(公告)日：2016-06-09
申请号：US15046357
申请日：2016-02-17
申请人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
发明人： Kevin C. Seavey , Walter C. Moore , John W. Weston , Carlos M. Villa
IPC分类号： C08G65/30
CPC分类号： C08G65/30 , B01D3/143 , B01D3/26 , B01D3/343 , B01D3/38
摘要： Organic materials are stripped and dried in a single column having two contact zones. A stripping gas is introduced into an upper contact zone and flows through the organic material in that zone. A drying gas is introduced into a lower contact zone. The drying gas contacts the organic material in both the upper and lower contact zones, and is removed from the top of the column together with the stripping gas. This process permits very efficiently removal of volatile organic compounds as well as efficient drying, while requiring on low levels of the stripping and drying gasses.
摘要翻译：将有机材料剥离并在具有两个接触区的单个柱中干燥。汽提气体被引入上部接触区域并流过该区域中的有机材料。干燥气体被引入下接触区域。干燥气体与上接触区域和下接触区域中的有机材料接触，并与汽提气体一起从柱顶部除去。该方法允许非常有效地除去挥发性有机化合物以及有效的干燥，同时需要低水平的汽提和干燥气体。

9. 发明申请

US20110105802A1 Continuous Loop Flow Process For Polyether Polyol Production 有权
标题翻译：聚醚多元醇生产的连续循环流程
公开(公告)号：US20110105802A1
公开(公告)日：2011-05-05
申请号：US12992025
申请日：2009-05-19
申请人： Carlos M. Villa , John W. Weston , Pradeep Jain , Leigh H. Thompson , Jean-Paul Masy
发明人： Carlos M. Villa , John W. Weston , Pradeep Jain , Leigh H. Thompson , Jean-Paul Masy
IPC分类号： C07C41/02 , B01J19/00
CPC分类号： C08G65/2663 , C08G65/2609 , C08G65/2696 , Y02P20/124
摘要： The present disclosure relates, according to some embodiments, to compositions, apparatus, methods, and systems that may be used to produce polyols, for example, polyether polyols with a narrow range of molecular weights, with little if any unsaturated byproducts, in a sustained and/or continuous reaction, with efficient heat transfer, and/or at high production rates. For example, in some embodiments, teachings of the disclosure may be used to produce polyether polyols in a continuous loop flow process. A continuous loop flow process may be practiced such that heat is effectively transferred and/or product properties (e.g., range of molecular weights) are controllable. For example, a continuous loop flow process may use one or more continuous flow loops comprising a heat exchanger, a means to move material around each loop, inlets for catalyst, monomer, initiator or starter, and an outlet for polyol product.
摘要翻译：根据一些实施方案，本公开涉及可用于制备多元醇的组合物，装置，方法和系统，例如具有窄范围分子量的聚醚多元醇，几乎没有不饱和副产物，在持续的和/或连续反应，有效的热传递和/或以高生产率。例如，在一些实施方案中，本公开的教导可用于在连续环流过程中制备聚醚多元醇。可以实践连续环流过程，使得有效地转移热量和/或产物性质（例如，分子量范围）是可控的。例如，连续环流过程可以使用一个或多个连续流动回路，其包括热交换器，用于在每个回路周围移动材料的装置，用于催化剂，单体，引发剂或起动器的入口以及多元醇产物的出口。

10. 发明授权

US09758619B2 Process for making polyether alcohols having oxyethylene units by polymerization of ethylene carbonate in the presence of double metal cyanide catalysts 有权
公开(公告)号：US09758619B2
公开(公告)日：2017-09-12
申请号：US14234577
申请日：2012-08-15
申请人： Esther E. Quintanilla , Hanno R. Van Der Wal , Daniel C. Floyd , Myriam Linke , Francois M. Casati , Carlos M. Villa , Jean-Paul Masy , Ricco B. Borella , Paul Cookson
发明人： Esther E. Quintanilla , Hanno R. Van Der Wal , Daniel C. Floyd , Myriam Linke , Francois M. Casati , Carlos M. Villa , Jean-Paul Masy , Ricco B. Borella , Paul Cookson
IPC分类号： C08G65/34 , C08G65/00 , C08G65/26
CPC分类号： C08G65/34 , C08G65/00 , C08G65/2663
摘要： Ethylene carbonate is polymerized by itself or together with another cyclic monomer such as 1,2-propylene oxide in the presence of a double metal cyanide catalyst. Most of the ethylene carbonate adds to the chain to form a terminal carbonate group, which decarboxylates to produce a hydroxyethyl group at the end of the polymer chain. The polymerization of more ethylene carbonate onto the chain end results in the formation of poly(ethyleneoxy) units. Therefore, the process provides a method for making poly(ethyleneoxy) polymers without the need to polymerize ethylene oxide. The process is useful for making polyethers that are useful as water-absorbable polymers, surfactants and as raw materials for polyurethanes. The process is also useful for increasing the primary hydroxyl content of a polyether.

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