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公开(公告)号:US08354083B2
公开(公告)日:2013-01-15
申请号:US12404531
申请日:2009-03-16
IPC分类号: B01J8/06
CPC分类号: B01J8/002 , B01J8/003 , B01J8/06 , B01J19/2485 , B01J2208/00752 , B01J2208/00769 , B01J2219/2443 , Y10T29/49345 , Y10T29/4984
摘要: Multi-tubular reactors for fluid processing incorporate reactor tubes containing thermally conductive monolithic catalyst structures with relative dimensions and thermal expansion characteristics effective to establish both a non-interfering or slidably interfering fit between the monolith structures and the reactor tubes at selected monolith mounting temperatures, and geometries at reactor operating temperatures such that the operating gaps between tubes and monoliths under the conditions of reactor operation do not exceed about 250 μm over tube sections where high heat flux to or from the monoliths is required.
摘要翻译: 用于流体处理的多管式反应器包括含有导热整体式催化剂结构的反应器管,其具有相对尺寸和热膨胀特性,有效地在选定的整料安装温度下建立整料结构和反应器管之间的非干扰或可滑动干扰的配合,以及 在反应器操作温度下的几何形状,使得在反应器操作条件下管和整料之间的操作间隙在需要高的热通量或来自整料的管段上不超过约250μm。
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公开(公告)号:US20090176895A1
公开(公告)日:2009-07-09
申请号:US12404531
申请日:2009-03-16
IPC分类号: C07B33/00 , C07D303/02 , C07C45/27 , C07D307/89 , C07D307/26 , C07C29/48 , B21D51/16 , B23P11/00
CPC分类号: B01J8/002 , B01J8/003 , B01J8/06 , B01J19/2485 , B01J2208/00752 , B01J2208/00769 , B01J2219/2443 , Y10T29/49345 , Y10T29/4984
摘要: Multi-tubular reactors for fluid processing incorporate reactor tubes containing thermally conductive monolithic catalyst structures with relative dimensions and thermal expansion characteristics effective to establish both a non-interfering or slidably interfering fit between the monolith structures and the reactor tubes at selected monolith mounting temperatures, and geometries at reactor operating temperatures such that the operating gaps between tubes and monoliths under the conditions of reactor operation do not exceed about 250 μm over tube sections where high heat flux to or from the monoliths is required.
摘要翻译: 用于流体处理的多管式反应器包括含有导热整体式催化剂结构的反应器管,其具有相对尺寸和热膨胀特性,有效地在选定的整料安装温度下建立整料结构和反应器管之间的非干扰或可滑动干扰的配合,以及 在反应器操作温度下的几何形状,使得在反应器操作条件下的管和整料之间的操作间隙在需要高的热通量或来自整料的管部分上不超过约250mum。
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