公开(公告)号：US5144091A

公开(公告)日：1992-09-01

申请号：US732910

申请日：1991-07-19

Applicant: Hans Martan ,  Ulrike Wegerle ,  Wilhelm Ruppel ,  Lothar Riekert ,  Dieter Becker ,  Michael Kotter

Inventor： Hans Martan ,  Ulrike Wegerle ,  Wilhelm Ruppel ,  Lothar Riekert ,  Dieter Becker ,  Michael Kotter

IPC: B01J23/88 ,  B01J23/887 ,  B01J27/19 ,  B01J27/192 ,  C07B61/00 ,  C07C45/35 ,  C07C47/22

CPC classification number: B01J27/192 ,  B01J23/002 ,  B01J23/8876 ,  C07C45/35 ,  B01J2523/00

Abstract: A process for the catalytic gas-phase oxidation of propene or isobutene to acrolein or methacrolein in a tubular fixed bed reactor or catalytically active oxides with a .gtoreq.90% conversion of the initial olefin on a single passage, wherein the temperature of the gases containing the reactants in the direction of flow along the tubes from their entrance until the conversion of the initial olefin is from 30 to 70% is from 360.degree. to 420.degree. C. and is then adjusted to from 360.degree. to 300.degree. C. until the conversion of the initial olefin is from 80 to 90% and is thereafter maintained at from 330.degree. to 390.degree. C. until the gases emerge from the tubes, is described.

Abstract translation: 在管式固定床反应器中催化气相氧化丙烯或异丁烯至丙烯醛或甲基丙烯醛的方法或在单一通道上具有初始烯烃转化率> 90％的催化活性氧化物的方法，其中气体的温度 在反应物的入口方向沿着管的流动方向含有反应物，直到初始烯烃的转化率为30-70％为360℃至420℃，然后调节至360℃至300℃直至 描述了初始烯烃的转化率为80-90％，然后保持在330℃至390℃，直到气体从管中出来。

公开(公告)号：US4867953A

公开(公告)日：1989-09-19

申请号：US006551

申请日：1986-12-11

Applicant: Lothar Riekert ,  Michael Kotter ,  Friedrich Weyland

Inventor： Lothar Riekert ,  Michael Kotter ,  Friedrich Weyland

IPC: B01D53/94 ,  B01D20060101 ,  B01D53/00 ,  B01D53/86

CPC classification number: B01D53/8625 ,  Y02C20/10

Abstract: Method for the selective elimination of nitrogen oxides from flue gases, especially from the flue gases from furnaces.For the denitration, the flue gases are brought together with catalytically active solid bodies through which the flue gases can flow on account of their structural makeup and/or because they are in the form of a loose bed. A reducing agent, mixed if desired with a carrier gas, is brought in contact with the catalytically active solid or sections thereof, in alternation with the flue gases containing the nitrogen oxides that are to be reduced.

Abstract translation: PCT No.PCT / EP86 / 00072 Sec。 371日期1986年12月11日第 102（e）日期1986年12月11日PCT提交1986年2月19日PCT公布。 第WO87 / 04947号公报 日期1987年8月27日。用于从烟道气，特别是来自炉的烟道气中选择性地除去氮氧化物的方法。 对于脱硝，烟气与催化活性的固体一起被带入，烟道气由于它们的结构组成和/或因为它们是松散床的形式而可以通过其流动。 如果需要，与载气混合的还原剂与含有待还原的氮氧化物的烟道气交替地与催化活性固体或其部分接触。

公开(公告)号：US4594332A

公开(公告)日：1986-06-10

申请号：US762026

申请日：1985-08-02

Applicant: Wolfgang Hoelderich ,  Lothar Riekert ,  Michael Kotter ,  Ulrich Hammon

Inventor： Wolfgang Hoelderich ,  Lothar Riekert ,  Michael Kotter ,  Ulrich Hammon

IPC: B01J29/40 ,  B01J37/00 ,  B01J29/28

CPC classification number: B01J37/0009 ,  B01J29/40

Abstract: Hard, fracture-resistant catalysts are prepared from zeolites of the pentasil family by a process in which water, organic additives which increase the viscosity and a silicate are added to the zeolite powder, and the material is molded, dried and calcined.The fracture-resistant zeolites obtained are used as catalyst carriers.

Abstract translation: 通过一种方法制备硬质，耐断裂的催化剂，其中将水，将粘度增加的有机添加剂和硅酸盐加入到沸石粉末中，并将该材料模制，干燥和煅烧。 所得到的耐断裂沸石用作催化剂载体。