公开(公告)号：AU7979801A

公开(公告)日：2002-03-13

申请号：AU7979801

申请日：2001-08-02

Applicant: DEGUSSA

Inventor： SCHUTTE RUDIGER ,  BALDUF TORSTEN ,  BECKER CATRIN ,  HEMME INA ,  BERTSCH-FRANK BIRGIT ,  WILDNER WERNER ,  ROLLMANN JURGEN ,  MARKOWZ GEORG

IPC: B01F5/00 ,  B01F5/04 ,  B01F13/00 ,  B01J3/04 ,  B01J8/00 ,  B01J8/02 ,  B01J19/00 ,  B01J19/24 ,  C01B15/029 ,  C07B61/00 ,  C07C45/35 ,  C07C47/21 ,  C07C47/22 ,  C07C51/25 ,  C07C57/04 ,  C07C57/05 ,  C07D301/12 ,  C07D303/04 ,  F28D9/00 ,  F28F3/12

Abstract: Two reactants are introduced into a slot-shaped reaction space (3) of a reactor. The space is formed between lateral surfaces (2) of two equally large and right parallelepipedal wall elements (1) comprising solid plates. The reactants are introduced from the edge of the slot-shaped reaction spaces situated on the same side of the block. Two reactants are introduced into a slot-shaped reaction space of a reactor. The spaces are formed between lateral surfaces of two equally large and right parallelepipedal wall elements comprising solid plates. The wall elements are arranged interchangeably in a block within the virtual parallelepiped. The reactants are introduced from edge regions of the slot-shaped reaction spaces situated on the same side of the block. The reactants are conducted as a reaction mixture through the reaction spaces in the same direction in parallel flows. A fluid heat exchange medium is conducted through tubular cavities (5) extending in the interior of the wall elements to obtain the desired reaction. An independent claim is also included for apparatus comprising the reactor in which the slot-shaped reaction spaces are capable of having the reactants supplied from the same side of the block. The reaction spaces are oriented to guide the reaction mixture in the same direction in parallel flows.

公开(公告)号：CA2420622A1

公开(公告)日：2002-03-07

申请号：CA2420622

申请日：2001-08-02

Applicant: DEGUSSA ,  UHDE GMBH

Inventor： MARKOWZ GEORG ,  BERTSCH-FRANK BIRGIT ,  SCHUTTE RUDIGER ,  BALDUF TORSTEN ,  HEMME INA ,  BECKER CATRIN ,  WILDNER WERNER ,  ROLLMANN JURGEN

IPC: B01F5/00 ,  B01F5/04 ,  B01F13/00 ,  B01J3/04 ,  B01J8/00 ,  B01J8/02 ,  B01J19/00 ,  B01J19/24 ,  C01B15/029 ,  C07B61/00 ,  C07C45/35 ,  C07C47/21 ,  C07C47/22 ,  C07C51/25 ,  C07C57/04 ,  C07C57/05 ,  C07D301/12 ,  C07D303/04 ,  F28D9/00 ,  F28F3/12

Abstract: Reactions between at least two fluid reactants are performed in a reactor comprising wall elements (1), slot-shaped reaction spaces (3) and cavities ( 5) for conducting a fluid heat-carrier through. Depending on the process and throughput, a modular structural design is chosen wherein an arbitrary numbe r of wall elements (1) are assembled to a right-parallelepipedal block (24), t he reaction spaces (3) are formed between lateral surfaces (2) of right- parallelepipedal wall elements (1), the reactants are introduced into the reaction spaces (3) from edge regions of one side of the block (24) and are conducted through the reaction spaces (3) in parallel flows and the fluid he at- carrier is conducted through the tubular cavities (5) extending in the interior of the wall elements (1).

公开(公告)号：ES2165236T3

公开(公告)日：2002-03-01

申请号：ES99919213

申请日：1999-03-31

Applicant: DEGUSSA

Inventor： BERTSCH-FRANK BIRGIT ,  BALDUF TORSTEN ,  BECKER-BALFANZ CATRIN ,  HEMME INA ,  ROLLMANN JURGEN ,  SCHUTTE RUDIGER

IPC: B01J8/02 ,  C01B15/029

Abstract: An aqueous solution of hydrogen peroxide is produced by direct synthesis from hydrogen and oxygen in the presence of a heterogeneous catalyst. According to the invention, a gas mixture comprising H2 and O2, essentially saturated or supersaturated with water (=containing fog) is fed into a reactor containing the catalyst. The volume ratio of the gas mixture fed in (standard liters per hour) to liquid removed (liters per hour) is adjusted to a value equal to or greater than 15,000, especially 20,000 to 50,000, and the gas mixture leaving the reactor is recycled after replenishment with H2, O2, and H2O vapor. Solutions with high H2O2 concentration can be obtained according to the invention without additional concentration.

公开(公告)号：CA2338104A1

公开(公告)日：2001-08-26

申请号：CA2338104

申请日：2001-02-23

Applicant: DEGUSSA

Inventor： SCHUTTE RUDIGER ,  HEMME INA ,  WILDNER WERNER ,  BALDUF TORSTEN ,  ROLLMANN JURGEN ,  BECKER CATRIN ,  KATUSIC STIPAN ,  BERTSCH-FRANK BIRGIT

IPC: B01J23/40 ,  B01J27/13 ,  B01J37/22 ,  C01B15/029 ,  B01J27/08

Abstract: The invention is relative to a method of producing hydrogen peroxide by dire ct synthesis in which hydrogen and oxygen are reacted in the presence of a heterogeneous, carrier-free or carrier-bound catalyst containing at least one noble metal i n the presence or absence of a solvent and to a catalyst for carrying out the method. The use of a halide promoter and/or of a mineral acid can be avoided by usin g a noble-metal catalyst containing an inorganic iodine compound in an amount corresponding to 0.01 to 15% by weight iodine relative to the noble-metal content.

公开(公告)号：ID27454A

公开(公告)日：2001-04-12

申请号：ID20002315

申请日：1999-03-31

Applicant: DEGUSSA

Inventor： BERTSCH-FRANK BIRGIT ,  BALDUF TORSTEN ,  BECKER-BALFANZ CATRIN ,  HEMME INA ,  ROLLMANN JURGEN ,  SCHUTTE RUDIGER ,  WILDNER WERNER

IPC: B01J8/02 ,  C01B15/029

Abstract: An aqueous solution of hydrogen peroxide is produced by direct synthesis from hydrogen and oxygen in the presence of a heterogeneous catalyst. According to the invention, a gas mixture comprising H2 and O2, essentially saturated or supersaturated with water (=containing fog) is fed into a reactor containing the catalyst. The volume ratio of the gas mixture fed in (standard liters per hour) to liquid removed (liters per hour) is adjusted to a value equal to or greater than 15,000, especially 20,000 to 50,000, and the gas mixture leaving the reactor is recycled after replenishment with H2, O2, and H2O vapor. Solutions with high H2O2 concentration can be obtained according to the invention without additional concentration.