公开(公告)号：US06699443B1

公开(公告)日：2004-03-02

申请号：US09154130

申请日：1998-09-16

申请人： Roland Hourticolon ,  Reinhard Eltner ,  Juergen Latzel ,  Gerd Goebel ,  Petro Mendia ,  Axel Geisler

发明人： Roland Hourticolon ,  Reinhard Eltner ,  Juergen Latzel ,  Gerd Goebel ,  Petro Mendia ,  Axel Geisler

IPC分类号： B01J808

CPC分类号： B01J8/1818 ,  B01J8/0278 ,  B01J8/065 ,  Y10T137/4238

摘要： A liquid distributor, for a substantially vertical reactor with a fixed bed catalyst, in the form of a channel distributor with drainage outlets and further comprising an internal cleaning mechanism with cleaning elements to be lowered into the openings of the drainage outlets, is disclosed.

摘要翻译： 公开了一种液体分配器，用于具有固定床催化剂的基本垂直的反应器，具有排放出口的通道分配器的形式，并且还包括具有要降低到排水出口的开口中的清洁元件的内部清洁机构。

公开(公告)号：US06619571B1

公开(公告)日：2003-09-16

申请号：US09731965

申请日：2000-12-07

申请人： Roland Hourticolon ,  Gerd Goebel ,  Franz-Josef Carduck ,  Juergen Latzel

发明人： Roland Hourticolon ,  Gerd Goebel ,  Franz-Josef Carduck ,  Juergen Latzel

IPC分类号： B02C1912

CPC分类号： B01J8/0025 ,  B01J8/06 ,  B01J2208/00761

摘要： A method for the removal of a spent catalyst from a fixed-bed reactor is disclosed, wherein a suction hose, in which a high pressure hose comprising a high-pressure nozzle is integrated, is introduced into the reactor, the catalyst is then size-reduced by water under high pressure passed through the nozzle, the catalyst/water mixture is removed under suction and is optionally collected in a separator.

摘要翻译： 公开了一种从固定床反应器中除去废催化剂的方法，其中将包含高压喷嘴的高压软管整合在一起的吸入软管被引入反应器中， 在通过喷嘴的高压下被水还原，在抽吸下除去催化剂/水混合物，并任选地收集在分离器中。

公开(公告)号：US06683224B1

公开(公告)日：2004-01-27

申请号：US10304445

申请日：2002-11-26

申请人： Roland Hourticolon ,  Guenther Demmering ,  Hans-Peter Kubersky ,  Lothar Friesenhagen ,  Friedrich Hommers ,  Juergen Latzel ,  Eberhard Peukert ,  Hans-Guenther Richard ,  Udo Kreutzer

发明人： Roland Hourticolon ,  Guenther Demmering ,  Hans-Peter Kubersky ,  Lothar Friesenhagen ,  Friedrich Hommers ,  Juergen Latzel ,  Eberhard Peukert ,  Hans-Guenther Richard ,  Udo Kreutzer

IPC分类号： C07C29136

CPC分类号： C07C29/149 ,  C07C31/125 ,  C07C33/02

摘要： Naturally occurring fats, oils and fatty derivatives are continuously hydrogenated to fatty alcohols in a fixed-bed reactor in the presence of hydrogen in excess and hydrogenation catalysts under static pressures of 50 to 300 bar and at temperatures of 160 to 320° C. The liquid product is cooled and the excess hydrogen is returned to the reactor entrance by a gas circulation pump as a recycle gas after separation of the liquid product. The expense involved in cooling and reheating the recycle gas is eliminated without any reduction in the quality of the fatty alcohol produced providing the recycle gas is returned to the reactor entrance without reheating and the hydrogenation reaction is carried out under static pressures of at least 200 bar.

摘要翻译： 天然存在的脂肪，油和脂肪衍生物在固定床反应器中在过量的氢气和氢化催化剂的存在下，在50至300巴的静态压力和160至320℃的温度下，连续氢化成脂肪醇。液体 产物被冷却，并且在分离液体产物之后，过量的氢气作为循环气体由气体循环泵返回到反应器入口。 除去循环气体的冷却和再加热所涉及的费用被消除，而不会降低所产生的脂肪醇的质量，提供循环气体将不再重新加热而返回到反应器入口，氢化反应在至少200巴的静压下进行 。