Fish protein hydrolysate production from sardine solid waste by crude pepsin enzymatic hydrolysis in a bioreactor coupled to an ultrafiltration unit

被引:73
作者
Benhabiles, M. S. [1 ]
Abdi, N. [1 ]
Drouiche, N. [1 ,3 ]
Lounici, H. [1 ]
Pauss, A. [2 ]
Goosen, M. F. A. [4 ]
Mameri, N. [2 ]
机构
[1] Natl Polytech Sch Algiers, Algiers, Algeria
[2] Univ Technol Compiegne, Dept Genie Chim, F-60205 Compiegne, France
[3] Silicon Technol Dev Unit UDTS, Merveilles 16000, Algeria
[4] Alfaisal Univ, Riyadh, Saudi Arabia
来源
MATERIALS SCIENCE & ENGINEERING C-MATERIALS FOR BIOLOGICAL APPLICATIONS | 2012年 / 32卷 / 04期
关键词
Enzyme; Protein hydrolysate; Ultrafiltration; Bioreactor; Biochemical engineering; Food processing; I-CONVERTING-ENZYME; INHIBITORY PEPTIDE; OPTIMIZATION; FLUX;
D O I
10.1016/j.msec.2012.02.013
中图分类号
TB3 [工程材料学]; R318.08 [生物材料学];
学科分类号
082905 [生物质能源与材料]; 100103 [病原生物学];
摘要
The aims of the study were to optimize the production a fish protein hydrolysate (FPH) by enzymatic hydrolysis of sardine solid waste using crude pepsin, and to scale up the process in a bioreactor coupled to an ultrafiltration unit for product recovery. Results showed that the crude pepsin prepared by autolysis of the mucous membranes of a sheep stomach at optimal conditions (i.e. pH = 1.5-2 and incubation time of 6 h) could be satisfactory used for the enzymatic hydrolysis of fish solid waste. The optimal conditions for enzymatic reaction were: temperature 48 degrees C, and pH 1.5. The scale up of the enzymatic hydrolysis and the coupling of the reactor an ultrafiltration unit to concentrate the hydrolysate gave good results with a rejection coefficient for the protein hydrolysate product in the range of 90%. The volumetric concentration factor was 2.5, with a permeate flux of 200 L m(-2) bar(-1). However, the results also suggest that the ultrafiltration product concentration process may be operating beyond the critical flux at which point irreversible membrane fouling occurs. (c) 2012 Elsevier B.V. All rights reserved.
引用
收藏
页码:922 / 928
页数:7
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