公开(公告)号：WO2009024446A3

公开(公告)日：2009-05-07

申请号：PCT/EP2008060121

申请日：2008-08-01

Applicant: BASF SE ,  TELES JOAQUIM HENRIQUE ,  GUMLICH KAI ,  SCHAEFER JOCHEN ,  OEHLENSCHLAEGER STEFFEN ,  LAMM STEPHAN ,  MERTEN ROLAND ,  SCHAEFER MARTIN ,  GROB RUEDIGER ,  EMNET UWE

Inventor： TELES JOAQUIM HENRIQUE ,  GUMLICH KAI ,  SCHAEFER JOCHEN ,  OEHLENSCHLAEGER STEFFEN ,  LAMM STEPHAN ,  MERTEN ROLAND ,  SCHAEFER MARTIN ,  GROB RUEDIGER ,  EMNET UWE

IPC: C07C51/235 ,  B01J8/22 ,  C07C53/124 ,  C07C53/126 ,  C07C53/128

CPC classification number: C07C51/235 ,  C07C53/124 ,  C07C53/128 ,  C07C53/122 ,  C07C53/126

Abstract: The invention relates to a process for the oxidation of organic compounds with oxygen in which, in a first step, the organic compound and at least some of the oxygen required for the oxidation are charged to a first reaction zone, where the first reaction zone is operated isothermally and back-mixed, and in a second step the reaction mixture from the first reaction zone is passed to a second reaction zone, where the second reaction zone is operated adiabatically. The invention further relates to a reactor for carrying out the process comprising at least one isothermal (3, 5) and one adiabatic (7) reaction zone which are arranged in a reactor jacket (8), where each isothermal reaction zone (3, 5) is configured in the form of a jet loop reactor and the adiabatic reaction zone (7) is configured as bubble column.

Abstract translation: 本发明涉及一种方法，用于与氧的有机化合物的氧化，其中在第一步骤中的有机化合物和至少所需的氧的氧化的一部分在第一反应区中添加，其中，所述第一反应区等温运行和返混，并且在 第二步骤中，从所述第二反应区绝热操作的第一反应区的反应混合物供入第二反应区。 本发明还涉及一种用于执行该方法的反应器，其包括至少一个等温（3,5）和绝热（7）反应区被布置在反应器容器（8）中，每个等温反应区（3,5）中的一个形式 喷射回路反应器被设计和绝热反应区（7）被设计为泡罩塔。

公开(公告)号：BRPI0815629A2

公开(公告)日：2015-02-18

申请号：BRPI0815629

申请日：2008-08-01

Applicant: BASF SE

Inventor： TELES JOAQUIM HENRIQUE ,  GUMLICH KAI ,  SCHAEFER JOCHEN ,  OEHLENSCHLAEGER STEFFAN ,  LAMM STEPHAN ,  MERTEN ROLAND ,  SCHAEFER MARTIN ,  GROB RUEDIGER ,  EMNET UWE

IPC: C07C51/235 ,  B01J8/22 ,  C07C53/124 ,  C07C53/126 ,  C07C53/128

Abstract: The invention relates to a process for the oxidation of organic compounds by means of oxygen, in which, in a first step, the organic compound and at least part of the oxygen required for the oxidation are introduced into a first reaction zone which is operated isothermally and with backmixing and, in a second step, the reaction mixture from the first reaction zone is introduced into a second reaction zone which is operated adiabatically. The invention further relates to a reactor for carrying out the process, which comprises at least one isothermal reaction zone (3, 5) and an adiabatic reaction zone (7) which are arranged in a reactor shell (8), with each isothermal reaction zone (3, 5) being configured in the form of a jet loop reactor and the adiabatic reaction zone (7) being configured as a bubble column.