THE EFFECT OF THE LEVEL OF MICROMIXING ON THE OPTIMAL-DESIGN OF CSTRS PERFORMING MICHAELIS-MENTEN REACTIONS

被引：4

作者：

MALCATA, FX

机构：

[1] Escola Superior de Biotecnologia, Universidade Católica Portuguesa, Porto

来源：

CANADIAN JOURNAL OF CHEMICAL ENGINEERING | 1990年 / 68卷 / 02期

关键词：

D O I：

10.1002/cjce.5450680221

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

An analytical formula for the calculation of the substrate conversion under complete segregation conditions in a CSTR performing a biochemical reaction following Michaëlis‐Menten kinetics is obtained. The errors on the expected conversion arising from using an optimal reactor design based on the assumption of complete micromixing conditions are discussed. Methods for the determination of the optimal reactor size profile for a series of CSTR's under complete segregation conditions are reported, using the minimum of the overall space time as the objective function. Copyright © 1990 Canadian Society for Chemical Engineering

引用

页码：330 / 336

页数：7

共 22 条

[1]

ARIMA K, 1964, GLOBAL IMPACTS APPLI, P278

[2]

Aris R., 1961, OPTIMAL DESIGN CHEM

[3]

Bailey J., 1986, BIOCH ENG FUNDAMENTA, DOI 10.1016/0168-3659(86)90022-2

[4]

Bard Y., 1974, NONLINEAR PARAMETER

[5]

Beyer W. H., 1978, CRC STANDARD MATH TA

[6] OPTIMAL CONTINUOUS FERMENTATION REACTOR DESIGN [J].

BISCHOFF, KB .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1966, 44 (05) :281-&

[7] CONTINUOUS FLOW SYSTEMS - DISTRIBUTION OF RESIDENCE TIMES [J].

DANCKWERTS, PV .

CHEMICAL ENGINEERING SCIENCE, 1953, 2 (01) :1-13

[8] GENERALIZED MIXING HISTORY MODEL OF AN IMPERFECTLY MIXED CSTR [J].

DUNN, RW ;

HSU, CC .

CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1973, 51 (03) :378-380

[9]

Gill P. E., 1981, PRACTICAL OPTIMIZATI

[10]

Hill C.G., 2014, INTRO CHEM ENG KINET

← 1 2 3 →