公开(公告)号：US06598547B1

公开(公告)日：2003-07-29

申请号：US09700243

申请日：2001-06-18

申请人： Freimut Marold ,  Friedrich Wilhelm

发明人： Freimut Marold ,  Friedrich Wilhelm

IPC分类号： F23G510

CPC分类号： B01J19/002 ,  B01J8/12 ,  B01J2208/00221 ,  B01J2208/00398 ,  B01J2208/00433 ,  B01J2208/00504 ,  B01J2208/00513 ,  B09B3/00 ,  B09B3/0083 ,  C04B33/1325 ,  F42B33/06 ,  F42B33/067 ,  F42D5/04 ,  Y02P40/69

摘要： The invention relates to a method for disposing of hazardous or high-energy materials, in which the latter are caused to undergo a reaction in a pressure-proof housing under controlled conditions, the end products of which reaction are non-hazardous, as well as an apparatus for disposing of hazardous or high-energy materials with a pressure-proof housing in which the materials may be caused to undergo a reaction under controlled conditions, the end products of which reaction are non-hazardous.

摘要翻译： 本发明涉及一种用于处置危险或高能材料的方法，其中后者在受控条件下在耐压壳体中进行反应，其最终产物的反应是无害的，以及 用于通过耐压壳体处理危险或高能材料的装置，其中材料可能在受控条件下经历反应，其最终产物的反应是无害的。

公开(公告)号：US4566886A

公开(公告)日：1986-01-28

申请号：US600059

申请日：1984-04-12

申请人： Rainer Fabian ,  Freimut Marold ,  Dieter Latzin

发明人： Rainer Fabian ,  Freimut Marold ,  Dieter Latzin

IPC分类号： C01B3/50 ,  C01B32/40 ,  F25J3/02 ,  F25J3/06

CPC分类号： C01B3/506 ,  C01B31/18 ,  F25J3/0223 ,  F25J3/0252 ,  F25J3/0261 ,  F25J3/0625 ,  F25J3/0655 ,  F25J3/0665 ,  C01B2203/047 ,  C01B2203/0475 ,  C01B2203/0495 ,  F25J2200/70 ,  F25J2205/04 ,  F25J2210/04 ,  F25J2230/30 ,  F25J2245/02 ,  F25J2270/02 ,  F25J2270/04 ,  F25J2270/08 ,  Y02C10/12 ,  Y10S62/92

摘要： For obtaining pure CO from a gaseous mixture, consisting predominantly of hydrogen and carbon monoxide, e.g., that produced by the endothermic catalytic oxidation of hydrocarbons in the presence of CO.sub.2 as the oxygen-yielding agent the gaseous mixture is compressed; residual CO.sub.2 and water are removed by adsorption; the resultant purified gaseous mixture is cooled to condense a predominant portion of CO; the condensed CO is pressure-reduced to remove dissolved H.sub.2 in the gaseous phase, the latter being recycled in gaseous form to the gaseous mixture; a fraction of the remaining liquid CO is partially vaporized and engine expanded to produce refrigeration for the system, and after engine expansion, is recycled to the gaseous mixture upstream of the compressor.

摘要翻译： 为了获得主要由氢气和一氧化碳组成的气态混合物的纯CO，例如通过在CO 2存在下通过烃的吸热催化氧化作为产生氧的试剂，气态混合物被压缩; 通过吸附除去残留的CO 2和水; 将所得纯化的气体混合物冷却以冷凝CO的主要部分; 冷凝的CO被压力降低以除去气相中的溶解的H 2，后者以气态形式再循环到气态混合物中; 剩余液体CO的一部分被部分蒸发并且发动机膨胀以产生用于该系统的制冷，并且在发动机膨胀之后，再循环到压缩机上游的气态混合物。

公开(公告)号：US4488890A

公开(公告)日：1984-12-18

申请号：US564868

申请日：1983-12-23

申请人： Wolfgang Foerg ,  Walter Scholz ,  Freimut Marold

发明人： Wolfgang Foerg ,  Walter Scholz ,  Freimut Marold

IPC分类号： F25J3/02 ,  F25J3/06 ,  F25J3/00 ,  B01D47/00

CPC分类号： F25J3/0271 ,  F25J3/0223 ,  F25J3/0233 ,  F25J3/0252 ,  F25J2200/76 ,  F25J2205/30 ,  F25J2215/02 ,  F25J2245/02 ,  F25J2270/04 ,  F25J2270/08

摘要： For the low-temperature separation of a gaseous mixture containing essentially hydrogen, C.sub.1+ -hydrocarbons, and carbon monoxide, resulting in a purified gaseous mixture to be processed, after the low-temperature separation, in methanol synthesis, the gaseous mixture is cooled and subsequently fed to a scrubbing column to scrub out the C.sub.1+ -hydrocarbons with liquid CO. A product containing essentially hydrogen and carbon monoxide is obtained at the head of the scrubbing column. The resultant liquid CO, loaded essentially with the C.sub.1+ -hydrocarbons, is withdrawn as the sump product from the column and introduced into a C.sub.1+ -CO separating column.

摘要翻译： 对于基本上含有氢气，C1 + - 碳氢化合物和一氧化碳的气态混合物的低温分离，在甲醇合成后，在低温分离后，得到待处理的纯化气态混合物，将气体混合物冷却 进料到洗涤塔以用液体CO洗涤C1 +烃。在洗涤塔的头部获得含有基本上氢和一氧化碳的产物。 基本上加入C1 +烃的所得液体CO作为贮槽产物从塔中取出并引入到C1 + -CO分离塔中。