Use of a two-phase reactor with pre-saturator for multiphase reactions

被引：4

作者：

Battsengel, B

Datsevich, L

Jess, A

Münnich, C

Peter, S

Turek, T

机构：

[1] Univ Bayreuth, Lehrstuhl Chem Verfahrenstech, D-95440 Bayreuth, Germany

[2] Bayer Technol Serv, BTS PT RPT REC, D-51368 Leverkusen, Germany

来源：

CHEMIE INGENIEUR TECHNIK | 2003年 / 75卷 / 05期

关键词：

D O I：

10.1002/cite.200390107

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：553 / 558

页数：6

共 8 条

[1]

Battsengel B, 2002, CHEM ENG TECHNOL, V25, P621, DOI 10.1002/1521-4125(200206)25:6<621::AID-CEAT621>3.0.CO

[2]

2-4

[3]

BATTSENGEL B, 2002, THESIS RWTH AACHEN A

[4] Multiphase reactors - revisited [J].

Dudukovic, MP ;

Larachi, F ;

Mills, PL .

CHEMICAL ENGINEERING SCIENCE, 1999, 54 (13-14) :1975-1995

[5]

JESS A, 2001, CHEM-ING-TECH, V73, P738

[6]

PETER S, 2001, THESIS RWTH AACHEN

[7] Process intensification in in-line monolithic reactor [J].

Stankiewicz, A .

CHEMICAL ENGINEERING SCIENCE, 2001, 56 (02) :359-364

[8] Catalytic hydrogenation reactors for the fine chemicals industries. Their design and operation [J].

Westerterp, KR ;

Molga, EJ ;

vanGelder, KB .

CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 1997, 36 (01) :17-27

← 1 →