-
公开(公告)号:US06221332B1
公开(公告)日:2001-04-24
申请号:US09129359
申请日:1998-08-05
IPC分类号: C01B3124
CPC分类号: B01J19/26 , B01F3/08 , B01F5/0256 , B01F13/0059 , B01J3/00 , B01J4/02 , B01J14/00 , B01J19/0093 , B01J23/80 , B01J2208/00672 , B01J2219/00162 , B01J2219/00164 , B01J2219/00889 , B01J2219/00891 , C01B13/36 , C01B13/363 , C01B33/26 , C01F11/181 , C01F11/462 , C01G1/02 , C01G9/006 , C01P2002/22 , C01P2002/72 , C01P2004/38 , C01P2004/52 , C01P2004/61 , C01P2004/62
摘要: Enhanced macromixing, mesomixing, and micromixing of multiple discrete reactant streams, particularly for precipitation reactions of low density pumpable fluids, are obtained by controlled continuous high pressure multiple reactant streams flowing into a chemical mixer/reactor. Individual reactant streams are pressurized to about 8,000 to 50,000 psi and achieve velocities up to about 250 meters/second in the final stage of the chemical mixer/reactor. Reactant flows are controlled by a combination of a fixed restriction and a variable driving pump.
摘要翻译: 通过流入化学混合器/反应器的受控的连续高压多反应物流,获得了多个不连续的反应物流,特别是用于低密度可泵送流体的沉淀反应的增强的宏观混合,介质混合和微混合。 单个反应物流被加压至约8,000至50,000psi,并且在化学搅拌器/反应器的最后阶段达到高达约250米/秒的速度。 反应物流由固定限制和可变驱动泵的组合控制。
-
公开(公告)号:US6159442A
公开(公告)日:2000-12-12
申请号:US129294
申请日:1998-08-05
申请人: Jeffrey R. Thumm , Michael A. Lento , Jerome S. Higgins , David Lassen King , David Mark Ginter , Laurent DAny Kieken
发明人: Jeffrey R. Thumm , Michael A. Lento , Jerome S. Higgins , David Lassen King , David Mark Ginter , Laurent DAny Kieken
IPC分类号: B01F3/08 , B01F5/02 , B01J3/00 , B01J4/02 , B01J14/00 , B01J19/00 , B01J19/26 , B01J23/80 , C01B13/36 , C01B33/26 , C01F11/18 , C01F11/46 , C01G1/02 , C01G9/00 , C01B3/12
CPC分类号: B01J19/26 , B01F5/0256 , B01J14/00 , B01J19/0093 , B01J23/80 , B01J3/00 , B01J4/02 , C01B13/36 , C01B13/363 , C01B33/26 , C01F11/181 , C01F11/462 , C01G1/02 , C01G9/006 , B01F13/0059 , B01F3/08 , B01J2208/00672 , B01J2219/00162 , B01J2219/00164 , B01J2219/00889 , B01J2219/00891 , C01P2002/22 , C01P2002/72 , C01P2004/38 , C01P2004/52 , C01P2004/61 , C01P2004/62
摘要: Processes for use of a controlled continuous high pressure multiple reactant streams flowing into a chemical mixer/reactor. Individual reactant streams are pressurized to about 8,000 to 50,000 psi and achieve velocities up to about 250 meters/second in the final stage of the chemical mixer/reactor.
摘要翻译: 使用流入化学混合器/反应器的受控连续高压多反应物流的方法。 单个反应物流被加压至约8,000至50,000psi,并且在化学搅拌器/反应器的最后阶段达到高达约250米/秒的速度。
-