Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
Product posters Crediblestirred tank bioreactor design reaction kettle high pressure reactor specification (L) Nominal diameter ( Phimm) nominal diameter of the jacket ( Phimm) Motor Power (KW) Reducer model Mixer speed (r.p. m) 30 400 500 0.6 BLD 0.6-1 60-100 50 500 600 0.8 BLD 0.8-1 60-100 100 550 650 1.1 BLD 1.1-1 60-100 150 600 700 2.2
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100l continuous stirred mixing bioreactor. Continuous Stirred Tank Reactoran overview . Continuous stirred tank reactor (CSTR) is the most generally employed bioreactor for biohydrogen production in continuous mode because of its simplicity in configuration easy functioning efficient uniform stirring and proper maintenance of temperature and pH (Fig. 10.2A) these types of bioreactors
100l continuous stirred mixing bioreactor. Continuous Stirred Tank Reactoran overview . Continuous stirred tank reactor (CSTR) is the most generally employed bioreactor for biohydrogen production in continuous mode because of its simplicity in configuration easy functioning efficient uniform stirring and proper maintenance of temperature and pH (Fig. 10.2A) these types of bioreactors
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Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
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100l continuous stirred mixing bioreactor. Continuous Stirred Tank Reactoran overview . Continuous stirred tank reactor (CSTR) is the most generally employed bioreactor for biohydrogen production in continuous mode because of its simplicity in configuration easy functioning efficient uniform stirring and proper maintenance of temperature and pH (Fig. 10.2A) these types of bioreactors
· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
Product posters Crediblestirred tank bioreactor design reaction kettle high pressure reactor specification (L) Nominal diameter ( Phimm) nominal diameter of the jacket ( Phimm) Motor Power (KW) Reducer model Mixer speed (r.p. m) 30 400 500 0.6 BLD 0.6-1 60-100 50 500 600 0.8 BLD 0.8-1 60-100 100 550 650 1.1 BLD 1.1-1 60-100 150 600 700 2.2
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· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
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Product posters Crediblestirred tank bioreactor design reaction kettle high pressure reactor specification (L) Nominal diameter ( Phimm) nominal diameter of the jacket ( Phimm) Motor Power (KW) Reducer model Mixer speed (r.p. m) 30 400 500 0.6 BLD 0.6-1 60-100 50 500 600 0.8 BLD 0.8-1 60-100 100 550 650 1.1 BLD 1.1-1 60-100 150 600 700 2.2
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Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
100l continuous stirred mixing bioreactor. Continuous Stirred Tank Reactoran overview . Continuous stirred tank reactor (CSTR) is the most generally employed bioreactor for biohydrogen production in continuous mode because of its simplicity in configuration easy functioning efficient uniform stirring and proper maintenance of temperature and pH (Fig. 10.2A) these types of bioreactors
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· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
Product posters Crediblestirred tank bioreactor design reaction kettle high pressure reactor specification (L) Nominal diameter ( Phimm) nominal diameter of the jacket ( Phimm) Motor Power (KW) Reducer model Mixer speed (r.p. m) 30 400 500 0.6 BLD 0.6-1 60-100 50 500 600 0.8 BLD 0.8-1 60-100 100 550 650 1.1 BLD 1.1-1 60-100 150 600 700 2.2
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Product posters Crediblestirred tank bioreactor design reaction kettle high pressure reactor specification (L) Nominal diameter ( Phimm) nominal diameter of the jacket ( Phimm) Motor Power (KW) Reducer model Mixer speed (r.p. m) 30 400 500 0.6 BLD 0.6-1 60-100 50 500 600 0.8 BLD 0.8-1 60-100 100 550 650 1.1 BLD 1.1-1 60-100 150 600 700 2.2
· Continuous hydrolysis of palm oil triglyceride in organic solvent using immobilized Candida rugosa on the Amberlite -1 as a source of immobilized lipase was studied in packed bed reactor. The enzymatic kinetics of hydrolysis reaction was studied by changing the substrate concentration reaction temperature and residence time(tau) in the reactor.
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Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
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100l continuous stirred mixing bioreactor. Continuous Stirred Tank Reactoran overview . Continuous stirred tank reactor (CSTR) is the most generally employed bioreactor for biohydrogen production in continuous mode because of its simplicity in configuration easy functioning efficient uniform stirring and proper maintenance of temperature and pH (Fig. 10.2A) these types of bioreactors
Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
Process Design for production of 2.4 kgannum of M72 Antigen from E. coli
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