公开(公告)号：US20110308932A1

公开(公告)日：2011-12-22

申请号：US13162601

申请日：2011-06-17

Applicant: Esa Tamminen ,  Matti Happonen ,  Ulla Happonen ,  Simo Jortikka ,  Martti Ruskoaho

Inventor： Esa Tamminen ,  Matti Happonen ,  Ulla Happonen ,  Simo Jortikka ,  Martti Ruskoaho

IPC: B01D3/10 ,  B01F3/04

CPC classification number: B01D3/008 ,  B01D1/06 ,  B01D3/06 ,  B01D3/14 ,  B01D3/20 ,  B01D3/32 ,  B01D19/0036 ,  B01D19/0063 ,  B01D19/0094

Abstract: The present invention relates to a feed distribution device in separation columns and a method of operation. In particular it relates to distillation columns in which the feed stream is substantially liquid phase, or a mixture of gas and liquid upstream of the column, but where the feed vaporizes or vaporizes more when it enters the column. More specifically, the feed distribution device contains a plurality of opening which allow the feed to vaporize inside the column and where the openings are maintained in critical condition during operation. Significant advantage is achieved through the implementation and use of the present feed distribution device.

Abstract translation: 本发明涉及分离塔中的进料分配装置和操作方法。 特别地，其涉及其中进料流基本上为液相的蒸馏塔，或塔的上游的气体和液体的混合物，但是当进料进入塔时进料蒸发或蒸发更多的蒸馏塔。 更具体地，进料分配装置包含多个开口，其允许进料在塔内蒸发，并且其中开口在操作期间保持在临界状态。 通过实施和使用本发明的饲料分配装置可以实现显着的优点。

公开(公告)号：US5254784A

公开(公告)日：1993-10-19

申请号：US811315

申请日：1991-12-20

Applicant: Matti Nurminen ,  Fredrik Nissfolk ,  Raimo Linnaila ,  Vesa-Matti Happonen

Inventor： Matti Nurminen ,  Fredrik Nissfolk ,  Raimo Linnaila ,  Vesa-Matti Happonen

IPC: B01J31/22 ,  B01J27/32 ,  C01B35/06 ,  C08F4/06 ,  C08F4/14 ,  C07C2/22

CPC classification number: B01J27/32

Abstract: The invention relates to a method for removing a boron trifluoride from the exhaust gases of a vacuum pump, which gases have been obtained when polymerizing .alpha.-olefines by using a BF.sub.3 -alcohol complex as a catalyst. In a vacuum distillation, the underpressure is achieved by means of a pump sealed with a fluid ring or by means of fluid jet with a torque or ejector pump, possibly assisted by a mechanical blaster, such as a propellant circulating pump. In this pump, the fluid ring or the fluid jet is formed by a cocatalyst forming a complex with the BF.sub.3 catalyst, which cocatalyst is an alcohol, preferably butanol.