Protease enzyme production in tray bioreactor using solid state fermentation process

Number of pages: 129 File Format: word File Code: 31803
Year: 2014 University Degree: Master's degree Category: Chemical - Petrochemical Engineering
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  • Summary of Protease enzyme production in tray bioreactor using solid state fermentation process

    Dissertation for receiving a master's degree

    in the field of chemical engineering, biotechnology orientation

    Abstract

    Microbial proteases are among the most important hydrolyzing enzymes, which account for about 60% of the global industrial enzyme market. have given In this research, synthesis of protease enzyme in solid state fermentation process using Bacillus bacteria. licheniformis was investigated. Various agricultural wastes and products including wheat bran, rice bran, bagasse, corn husk, corn flour and barley flour were used as substrates. Protease produced from wheat husk has shown more activity than other substrates. The effect of different extraction parameters, including the type and amount of extractant solution and residence time in the shaker, was evaluated. The highest amount of protease recovery was obtained using 50 ml Tris buffer after 1 hour in the shaker. In addition, the effect of operating parameters such as time, temperature, pH, initial humidity, cabin humidity, particle size and amount of inoculum on enzyme production was investigated. The results showed that the highest amount of protease enzyme activity was obtained after 48 hours of fermentation at a temperature of 35°C, initial pH of 9, cabin humidity of 90%, particle size in the range of 1-2 cm, and initial humidity of 200% for the upper tray and 150% for the middle tray. Also, the effect of different carbon and nitrogen supplements on protease production was investigated. The results showed that by enriching the substrate with rice bran (1% w/w) and corn flour (2% w/w), the highest activity of protease enzyme was obtained. The maximum protease activity after 48 hours, under all optimal conditions, the activity level of 1281/1281 U/gds and 1048/7 U/gds was obtained for the upper and middle tray, respectively. The effect of temperature and pH on enzyme activity and stability was investigated. The results showed that the produced protease had an alkaline nature and had a very significant stability in the range of temperature changes in the range of 30-85 C? and pH values ??between 7-13, and the highest activity was obtained at a pH value of 8 and a temperature of 65 C?. Also, the use of produced enzyme in leather processing and hydrolysis of gelatin layer from photographic films and also as an additive to detergent was investigated. The results showed that the alkaline protease obtained from B. licheniformis showed a very good ability to remove various stains from fabric, remove hair from cow skin and digest the gelatin layer of photographic films. Also, the production of protease enzyme using solid state fermentation process in bioreactor and flask was investigated and the two systems were compared in terms of enzyme production rate.

    Key words: protease, wheat bran, solid state fermentation, tray bioreactor, Bacillus. licheniformis

    1-1. Introduction

    In this chapter, general explanations about enzymes, their structure and characteristics are discussed. Then the enzyme groups and related reactions are expressed. Brief information about proteases as one of the most important enzyme groups is mentioned below. Then the solid state fermentation process is introduced as an efficient fermentation system. At the end, the needs and goals of this project are discussed.

    1-2. Enzyme definition

    Enzymes are the most important group of proteins that are responsible for carrying out biochemical reactions and speeding them up and can increase the speed of the reaction up to 107 times. Enzymes are produced by living organisms, plants and microorganisms. Carrying out all reactions in a living cell requires a special enzyme. As shown in figure (1-1), enzyme like an inorganic catalyst is not consumed in the reaction but provides a lower energy pathway for the reaction to take place [1, 2]. Catalysts remain unchanged in reactions, but enzymes, like other proteins, do not remain stable under different conditions. Some enzymes are mainly active in a limited range of pH, temperature and ionic strength, and at temperatures and pHs higher than the optimum, the enzyme is destroyed and loses its activity [3, 4]. Due to the special conditions of many of these enzymes, they are not recommended for industrial use, so trying to find new species that meet the needs of the industry is a continuous process [5].

    1-3.Enzyme history

    The catalytic activity of enzymes has been used for thousands of years in various processes such as making cheese, wine and bakery [6]. By the 19th century, it was known that processes such as the souring of milk and the fermentation of sugar into alcohol could only occur through the action of a living organism. In 1833, the sugar activating agent was relatively purified and named diastase [1], which is now called amylase [2]. A few years later, they isolated a substance from the gastric juice of a person who was on a protein diet and named it pepsin [3]. These compounds are called under the general name of yeast. Liebig [4] stated at that time that these yeasts could be non-living materials derived from living cells, while Pasteur [5] and others still believed that yeasts must contain living materials. Despite these disagreements, Cohen [6] called these molecules enzymes in 1878. Buchners[7] showed in 1897 that when yeast extract is added to sugar, sugar fermentation takes place. In 1926, Sumner [8] purified urease enzyme [9] from bean extract and crystallized it. Since then, they were able to crystallize a large number of enzymes [7, 8]. Simultaneously with the emergence of the knowledge of enzyme purification, their applications multiplied and, of course, with the use of engineered enzymes, the number of choices for industrial processes increased [6]

    Abstract

     

    Microbial protease is one of the most important enzymes and represents 60% of total industrial enzyme sales. In this study, protease synthesis in solid state fermentation using B. licheniformis was investigated. Several agricultural residues such as rice bran, sugarcane bagasse, wheat bran, barely bran, corn meal and corn husk were used as substrates. Protease from the wheat bran showed higher activities than other substrates. Effect of extraction parameters such as type and volume of extracted medium and mixing time in shaker were investigated. Maximum recovery of protease obtained with 50 ml of Tris-HCl buffer after 1 hour incubation in the incubator-shaker. Furthermore, the influence of operational parameters such as fermentation time, temperature, pH, initial moisture, cabin humidity, particle size and inoculum level were studied. Results showed that maximum activity of protease was obtained after 48h of incubation, cabin temperature of 35 °C, initial pH of 9, cabin humidity of 90%, particle size in the range of 1-2 cm and initial moisture of 200% for the top tray and 150% for the middle tray. Moreover, the effect of different carbon and nitrogen supplementary sources for protease production was investigated. Results showed that, maximum protease activity was obtained with supplementation of substrate with rice bran (1% w/w) and corn meal (2% w/w). Maximum protease activities achieved under all of the desired conditions were 1281.1 and 1048.7 U/gds for the top and middle trays respectively. Effect of temperature and pH for protease activity and thermal stability was investigated. The results showed that, the enzyme found to be a typical alkaline protease which was stable in broad temperature range (30-85 ?C) and pH values ??(7-13), with maximum activity was defined at 65 ?C and pH value of 8. Moreover, the application of produced enzyme in leather processing, hydrolysis of gelatin layers of photographic films and also an additive in detergents were investigated. Results showed that, alkaline protease from B. licheniformis, have variety of application in detergent formulation for the removal of stained from cotton cloths, dehairing of cow hide and hydrolysis of gelatin layers of photographic films. Also, protease production in two solid state fermentation systems including flask and bioreactor were evaluated. Finally, the protease production in two systems was compared.

    Key words: protease, wheat bran, solid state fermentation, tray bioreactor, Bacillus.

  • Contents & References of Protease enzyme production in tray bioreactor using solid state fermentation process

    List:

    Chapter 1 1

    Introduction 1

    1-1. Introduction. 2

    1-2. Enzyme definition. 2

    1-3. Enzyme history. 2

    1-4. Enzyme structure. 4

    1-5. Classification of enzymes 5

    1-6. History of protease enzyme 6

    1-7. The function of proteases 6

    1-8. Solid state fermentation. 7

    1-9. The need to do the project. 8

    1-10. The goals of this project. 8

    Chapter 2 review of study sources 10

    2-1. Introduction. 11

    2-2. Proteases 11

    2-3. Sources of proteases 12

    2-3-1. Plant proteases. 12

    2-3-2. Animal proteases. 13

    2-3-3. Microbial proteases. 13

    2-4. Classification of proteases 16

    2-5. Alkaline proteases. 19

    2-6. Mechanism of action of proteases 22

    2-7. Industrial applications of protease enzyme 22

    2-7-1. Detergent industry. 23

    2-7-2. Food industry. 24

    2-7-3. leather industry 25

    2-7-4. Photography industry. 26

    2-7-5. Pharmaceutical industry. 26

    2-7-6. Environmental management. 27

    2-8. Production of protease enzyme 27

    2-9. Submerged Fermentation 28

    2-9-1. Solid state fermentation. 29

    2-9-2. Comparison of solid and submerged fermentation systems 29

    2-9-3. Mass transfer in solid state fermentation. 30

    2-9-4. Macroscale mass transfer operations. 31

    2-9-5. Micro-scale mass transfer operations. 32

    2-9-6. Oxygen transfer. 32

    2-9-7. Penetration of enzymes 33

    2-9-8. Aspects of heat transfer. 34

    2-9-9. Microorganisms used in solid state fermentation. 35

    2-9-10. Applications of solid state fermentation. 37

    2-9-11. Enzymes obtained from the solid fermentation process. 38

    2-10. Bioreactor design 39

    2-11. Types of bioreactors used in solid state fermentation. 40

    2-11-1. Tray bioreactors 41

    2-11-2. Filled bed bioreactors 42

    2-11-3. Rotating cylindrical bioreactors 43

    2-11-4. Fluidized bed bioreactors. 45

    2-12. General steps for conducting the SSF process inside the bioreactor 46

    2-13. Effective factors in the production of protease in the SSF process inside the bioreactor 47

    Chapter 3 Materials and methods 48

    3-1. Introduction. 49

    3-2. Equipment used. 49

    3-3. Determining the characteristics of the substrate 50

    3-3-1. Calculate the amount of ash. 50

    3-3-2. Calculate the amount of moisture. 51

    3-3-3. Calculating the amount of sugar in the substrate 51

    3-3-4. Calculate the amount of protein. 52

    3-3-5. Determining the percentage of extractive materials. 54

    3-3-6. Determination of cellulose percentage. 54

    3-3-7. Determination of lignin percentage. 55

    3-3-8. Determination of hemicellulose percentage. 55

    3-3-9. Calculation of substrate particle size 55

    3-4. Microorganism and culture medium. 56

    3-4-1. Microorganism selection. 56

    3-4-2. Characteristics of the microorganism. 57

    3-4-3. Cultivation environment. 57

    3-4-4. Preparation of inoculum. 59

    3-4-5. Bacterial growth curve. 60

    3-4-6. Determining the optimal pH of bacteria. 60

    3-5. Solid state fermentation. 61

    3-6. Sampling and enzyme extraction from the fermented substrate. 63

    3-7. Protease activity 64

    3-7-1. Tyrosine standard curve. 65

    3-8. Investigating the effect of different parameters on the production of protease enzyme in tray bioreactor 66

    3-8-1. The effect of the type of solid substrate. 66

    3-8-2. Effect of fermentation time. 67

    3-8-3. Effect of temperature 67

    3-8-4. Effect of pH. 67

    3-8-5. Effect of different parameters on enzyme extraction. 68

    3-8-6. The effect of the initial humidity of the substrate 68

    3-8-7. The effect of the internal humidity of the reactor 68

    3-8-8. Effect of particle size. 68

    3-8-9. Effect of inoculation rate. 69

    3-8-10. Effect of substrate enrichment with carbon and nitrogen sources. 69

    3-8-11. The effect of pH on the activity and stability of the produced enzyme. 69

    3-8-12. The effect of temperature on the activity and stability of the produced enzyme. 70

    3-9. Production enzyme applications. 71

    3-9-1. Additive to detergents. 71

    3-9-2. Leather processing. 71

    3-9-3. Hydrolysis of the gelatin layer of photographic films and release of silver. 72

    3-10. Comparison of protease enzyme production in bioreactor and flask. 72

    Chapter 4 Results and72

    Chapter 4 Results and their interpretation 73

    4-1. Introduction. 74

    4-2. Calculation of wheat bran properties. 74

    4-3. Bacterial growth curve. 75

    4-4. Optimal pH for bacterial growth. 75

    4-5. Investigation of different parameters on the production of protease 76

    4-5-1. Effect of fermentation time. 76

    4-5-2. Investigation of the effect of the type of solid substrate. 78

    4-5-3. Investigating parameters affecting the extraction of protease 79

    4-5-4. Effect of initial pH. 82

    4-5-5. Checking the temperature inside the bioreactor 82

    4-5-6. The effect of the initial humidity of the substrate 84

    4-5-7. The influence of the internal humidity of the bioreactor 85

    4-5-8. Effect of particle size. 86

    4-5-9. The effect of the amount of inoculum. 87

    4-5-10. Investigating the effect of enriching the substrate with carbon and nitrogen sources. 87

    4-6. Optimizing enzyme protease activity conditions. 92

    4-6-1. Determining the optimal pH of enzyme activity. 92

    4-6-2. Determining the optimal temperature of enzyme activity. 94

    4-6-3. pH determination of enzyme stability. 95

    4-6-4. Determining the optimal temperature of enzyme stability. 96

    4-7. Applications of alkaline protease enzyme obtained from B. licheniformis. 97

    4-7-1. Alkaline protease function as a detergent additive. 97

    4-7-2. Depilation of the skin. 98

    4-7-3. Hydrolysis of the gelatin layer of X-Ray films. 99

    4-8. Comparison of protease enzyme production in bioreactor and flask. 100

    Chapter 5 conclusions and suggestions 103

    5-1. conclusion 104

    5-2. Suggestions 106

     

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Protease enzyme production in tray bioreactor using solid state fermentation process