1
|
Sadaqat B, Dar MA, Sha C, Abomohra A, Shao W, Yong YC. Thermophilic β-mannanases from bacteria: production, resources, structural features and bioengineering strategies. World J Microbiol Biotechnol 2024; 40:130. [PMID: 38460032 DOI: 10.1007/s11274-024-03912-4] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 12/01/2023] [Accepted: 01/29/2024] [Indexed: 03/11/2024]
Abstract
β-mannanases are pivotal enzymes that cleave the mannan backbone to release short chain mannooligosaccharides, which have tremendous biotechnological applications including food/feed, prebiotics and biofuel production. Due to the high temperature conditions in many industrial applications, thermophilic mannanases seem to have great potential to overcome the thermal impediments. Thus, structural analysis of thermostable β-mannanases is extremely important, as it could open up new avenues for genetic engineering, and protein engineering of these enzymes with enhanced properties and catalytic efficiencies. Under this scope, the present review provides a state-of-the-art discussion on the thermophilic β-mannanases from bacterial origin, their production, engineering and structural characterization. It covers broad insights into various molecular biology techniques such as gene mutagenesis, heterologous gene expression, and protein engineering, that are employed to improve the catalytic efficiency and thermostability of bacterial mannanases for potential industrial applications. Further, the bottlenecks associated with mannanase production and process optimization are also discussed. Finally, future research related to bioengineering of mannanases with novel protein expression systems for commercial applications are also elaborated.
Collapse
Affiliation(s)
- Beenish Sadaqat
- Biofuels Institute, School of the Environment and Safety Engineering, Jiangsu University, Zhenjiang, 212013, Jiangsu province, People's Republic of China
- Department of Biochemistry and Structural Biology, Lund University, Box 124, 22100, Lund, Sweden
| | - Mudasir A Dar
- Biofuels Institute, School of the Environment and Safety Engineering, Jiangsu University, Zhenjiang, 212013, Jiangsu province, People's Republic of China
| | - Chong Sha
- Biofuels Institute, School of the Environment and Safety Engineering, Jiangsu University, Zhenjiang, 212013, Jiangsu province, People's Republic of China
| | - Abdelfatah Abomohra
- Aquatic Ecophysiology and Phycology, Department of Biology, Institute of Plant Science and Microbiology, University of Hamburg, Hamburg, 22609, Germany
| | - Weilan Shao
- Biofuels Institute, School of the Environment and Safety Engineering, Jiangsu University, Zhenjiang, 212013, Jiangsu province, People's Republic of China.
| | - Yang-Chun Yong
- Biofuels Institute, School of the Environment and Safety Engineering, Jiangsu University, Zhenjiang, 212013, Jiangsu province, People's Republic of China.
| |
Collapse
|
2
|
Production of Polyhydroxyalkanoates through Soybean Hull and Waste Glycerol Valorization: Subsequent Alkaline Pretreatment and Enzymatic Hydrolysis. FERMENTATION-BASEL 2022. [DOI: 10.3390/fermentation8090433] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
Abstract
Alkaline pretreatment and sequential enzymatic hydrolysis of soybean hull were investigated to obtain fermentable sugars for polyhydroxyalkanoates production along with residual glycerol as low-cost carbon sources. Soybean hull is composed of approximately 32% cellulose, 12% hemicellulose, 6% lignin, and 11% protein. Alkaline pretreatment was carried out with 2% NaOH concentration, 10% (w/v) biomass loading, and 60 min incubation time in an autoclave at 120 °C. The response surface methodology (RSM) based on the central composite design (CCD) tool was employed to optimize the enzymatic hydrolysis process, where the variables of biomass loading, enzymes’ concentration, and time were considered. The maximum total reducing sugars concentration obtained was 115.9 g∙L−1 with an enzyme concentration of 11.5 mg protein/g dry substrate for enzyme preparation B1, 2.88 mg protein/g dry substrate for XylA, and 57.6 U/g dry substrate for β-glucosidase, after 42 h at 45 °C, and pH was 4.5. Subsequently, the saccharification step was conducted by increasing the processing scale, using a 1 L tank with stirring with a controlled temperature. Implementing the same enzyme concentrations at pH 4.5, temperature of 45 °C, 260 mL working volume, and incubation time of 42 h, under fed-batch operation with substrate feeding after 14 h and 22 h, a hydrolysate with a concentration of 185.7 g∙L−1 was obtained. Initially, to verify the influence of different carbon sources on Cupriavidus necator DSMz 545 in biomass production, batch fermentations were developed, testing laboratory-grade glucose, soybean hull hydrolysate, and waste glycerol (a by-product of biodiesel processing available in large quantities) as carbon sources in one-factor-at-a-time assays, and the mixture of soybean hull hydrolysate and waste glycerol. Then, the hydrolysate and waste glycerol were consumed by C. necator, producing 12.1 g∙L−1 of biomass and achieving 39% of polyhydroxyalkanoate (PHB) accumulation. To the best of our knowledge, this is the first time that soybean hull hydrolysate has been used as a carbon source to produce polyhydroxyalkanoates, and the results suggest that this agro-industrial by-product is a viable alternative feedstock to produce value-added components.
Collapse
|
3
|
Semenova MV, Gusakov AV, Telitsin VD, Matys VY, Bubnova TV, Nemashkalov VA, Rozhkova AM, Sinitsyn AP. A New Enzyme Preparation Containing Polysaccharide Monooxygenase and β-Glucosidase—Synergistic Additives to Cellulases. APPL BIOCHEM MICRO+ 2022. [DOI: 10.1134/s0003683822040147] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
|
4
|
Karp SG, Rozhkova AM, Semenova MV, Osipov DO, de Pauli STZ, Sinitsyna OA, Zorov IN, de Souza Vandenberghe LP, Soccol CR, Sinitsyn AP. Designing enzyme cocktails from Penicillium and Aspergillus species for the enhanced saccharification of agro-industrial wastes. BIORESOURCE TECHNOLOGY 2021; 330:124888. [PMID: 33713945 DOI: 10.1016/j.biortech.2021.124888] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 01/20/2021] [Revised: 02/16/2021] [Accepted: 02/17/2021] [Indexed: 06/12/2023]
Abstract
The aim of this study was to develop optimized enzyme cocktails, containing native and recombinant purified enzymes from five fungal species, for the saccharification of alkali- and acid-pretreated sugarcane bagasse (SCB), soybean hulls (SBH) and oil palm empty fruit bunches (EFB). Basic cellulases were represented by cellobiohydrolase I (CBH) and endo-glucanase II (EG) from Penicillium verruculosum and β-glucosidase (BG) from Aspergillus niger. Auxiliary enzymes were represented by endo-xylanase A (Xyl), pectin lyase (PNL) and arabinoxylanhydrolase (AXH) from Penicillium canescens, β-xylosidase (BX) from Aspergillus japonicus, endo-arabinase (ABN) from A. niger and arabinofuranosidase (Abf) from Aspergillus foetidus. Enzyme loads were 5 mg protein/g dry substrate (basic cellulases) and 1 mg/g (each auxiliary enzyme). The best choice for SCB and EFB saccharification was alkaline pretreatment and addition of Xyl + BX, AXH + BX or ABN + BX + Abf to basic cellulases. For SBH, acid pretreatment and basic cellulases combined with ABN + BX + Abf or Xyl + BX performed better than other enzyme preparations.
Collapse
Affiliation(s)
- Susan G Karp
- Federal University of Paraná, Department of Bioprocess Engineering and Biotechnology, 81531-990 Curitiba, Paraná, Brazil
| | - Alexandra M Rozhkova
- Federal Research Centre Fundamentals of Biotechnology» of the Russian Academy of Sciences, Moscow 119071, Russia.
| | - Margarita V Semenova
- Federal Research Centre Fundamentals of Biotechnology» of the Russian Academy of Sciences, Moscow 119071, Russia
| | - Dmitrii O Osipov
- Federal Research Centre Fundamentals of Biotechnology» of the Russian Academy of Sciences, Moscow 119071, Russia
| | - Suellen T Z de Pauli
- Federal University of Paraná, Postgraduate Program in Numerical Methods, Curitiba, Paraná, Brazil
| | - Olga A Sinitsyna
- M. V. Lomonosov Moscow State University, Department of Chemistry, Moscow 119991, Russia
| | - Ivan N Zorov
- Federal Research Centre Fundamentals of Biotechnology» of the Russian Academy of Sciences, Moscow 119071, Russia; M. V. Lomonosov Moscow State University, Department of Chemistry, Moscow 119991, Russia
| | | | - Carlos R Soccol
- Federal University of Paraná, Department of Bioprocess Engineering and Biotechnology, 81531-990 Curitiba, Paraná, Brazil.
| | - Arkady P Sinitsyn
- Federal Research Centre Fundamentals of Biotechnology» of the Russian Academy of Sciences, Moscow 119071, Russia; M. V. Lomonosov Moscow State University, Department of Chemistry, Moscow 119991, Russia.
| |
Collapse
|