DEGRADATION OF AROMATIC-COMPOUNDS BY PSEUDOMONAS-PUTIDA

被引：5

作者：

DLUHY, M ^{[1
]}

SEFCIK, J ^{[1
]}

BALES, V ^{[1
]}

机构：

[1] SLOVAK UNIV TECHNOL BRATISLAVA, FAC CHEM TECHNOL, DEPT CHEM & BIOCHEM ENGN, RADLINSKEHO 9, CS-81237 BRATISLAVA, CZECHOSLOVAKIA

来源：

ACTA BIOTECHNOLOGICA | 1993年 / 13卷 / 04期

关键词：

D O I：

10.1002/abio.370130405

中图分类号：

Q81 [生物工程学（生物技术）]; Q93 [微生物学];

学科分类号：

071005 ; 0836 ; 090102 ; 100705 ;

摘要：

The influence of different process kinetics on the course of phenol degradation has been studied as well as the influence of axial dispersion in the liquid phase on the reactor height with relatively large biofilm thickness in a conventional fluidized bed and air-lift bioreactor. The object of this was to achieve a high conversion of substrate in a device of real size in real process time. For calculating the mathematical model, the method of orthogonal collocation with the STIFF integration routine has been used.

引用

页码：333 / 340

页数：8

共 6 条

[1] APPLICATION OF ORTHOGONAL COLLOCATIONS TO SOME TRANSPORT PHENOMENA PROBLEMS IN COAXIAL CYLINDERS AND SPHERES [J].

GOYAL, SK ;

ESMAIL, MN ;

BAKHSHI, NN .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1987, 65 (05) :833-844

[2] OXIDATION OF AN INHIBITORY SUBSTRATE BY WASHED CELLS (OXIDATION OF PHENOL BY PSEUDOMONAS-PUTIDA) [J].

SOKOL, W .

BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (08) :921-927

[3] STEADY-STATE PHENOL DEGRADATION IN A DRAFT-TUBE, GAS-LIQUID-SOLID FLUIDIZED-BED BIOREACTOR [J].

TANG, WT ;

FAN, LS .

AICHE JOURNAL, 1987, 33 (02) :239-249

[4]

Villadsen J., 1977, SOLUTION DIFFERENTIA

[5] BIOLOGICAL PHENOL DEGRADATION IN A GAS-LIQUID-SOLID FLUIDIZED-BED REACTOR [J].

WISECARVER, KD ;

FAN, LS .

BIOTECHNOLOGY AND BIOENGINEERING, 1989, 33 (08) :1029-1038

[6] OPTIMUM PARTICLE-SIZE IN A GAS-LIQUID SOLID FLUIDIZED-BED CATALYTIC REACTOR [J].

WISECARVER, KD ;

FAN, LS .

CHEMICAL ENGINEERING SCIENCE, 1988, 43 (10) :2741-2750

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