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Narisetty V, Okibe MC, Amulya K, Jokodola EO, Coulon F, Tyagi VK, Lens PNL, Parameswaran B, Kumar V. Technological advancements in valorization of second generation (2G) feedstocks for bio-based succinic acid production. BIORESOURCE TECHNOLOGY 2022; 360:127513. [PMID: 35772717 DOI: 10.1016/j.biortech.2022.127513] [Citation(s) in RCA: 13] [Impact Index Per Article: 6.5] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/29/2022] [Revised: 06/21/2022] [Accepted: 06/22/2022] [Indexed: 06/15/2023]
Abstract
Succinic acid (SA) is used as a commodity chemical and as a precursor in chemical industry to produce other derivatives such as 1,4-butaneidol, tetrahydrofuran, fumaric acid, and bio-polyesters. The production of bio-based SA from renewable feedstocks has always been in the limelight owing to the advantages of renewability, abundance and reducing climate change by CO2 capture. Considering this, the current review focuses on various 2G feedstocks such as lignocellulosic biomass, crude glycerol, and food waste for cost-effective SA production. It also highlights the importance of producing SA via separate enzymatic hydrolysis and fermentation, simultaneous saccharification and fermentation, and consolidated bioprocessing. Furthermore, recent advances in genetic engineering, and downstream SA processing are thoroughly discussed. It also elaborates on the techno-economic analysis and life cycle assessment (LCA) studies carried out to understand the economics and environmental effects of bio-based SA synthesis.
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Affiliation(s)
- Vivek Narisetty
- School of Water, Energy and Environment, Cranfield University, Cranfield MK43 0AL, UK
| | | | - K Amulya
- National University of Ireland Galway, University Road, H91TK33 Galway, Ireland
| | | | - Frederic Coulon
- School of Water, Energy and Environment, Cranfield University, Cranfield MK43 0AL, UK
| | - Vinay Kumar Tyagi
- Environmental Hydrology Division, National Institute of Hydrology (NIH), Roorkee 247667, Uttarakhand, India
| | - Piet N L Lens
- National University of Ireland Galway, University Road, H91TK33 Galway, Ireland
| | - Binod Parameswaran
- Microbial Processes and Technology Division, CSIR - National Institute for Interdisciplinary Science and Technology, Trivandrum, Kerala 695019, India
| | - Vinod Kumar
- School of Water, Energy and Environment, Cranfield University, Cranfield MK43 0AL, UK.
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Assessment of vine shoots and surplus grape must for succinic acid bioproduction. Appl Microbiol Biotechnol 2022; 106:4977-4994. [PMID: 35821430 DOI: 10.1007/s00253-022-12063-1] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 01/04/2022] [Revised: 06/28/2022] [Accepted: 07/02/2022] [Indexed: 11/02/2022]
Abstract
Vine shoots and surplus grape must were assessed as feedstocks for succinic acid production with Actinobacillus succinogenes and Basfia succiniproducens. After acidic and enzymatic hydrolysis, vine shoots released 35-40 g/L total sugars. Both bacterial species produced 18-21 g/L succinic acid from this hydrolysate in 120 h. Regarding grape must fermentation, A. succinogenes clearly outperformed B. succiniproducens. Yeast extract (a source of organic nitrogen and vitamins) was the only additional nutrient needed by A. succinogenes to grow on grape must. Under mathematically optimized conditions (145.7 g/L initial sugars and 24.9 g/L yeast extract), A. succinogenes generated 88.9 ± 1.4 g/L succinic acid in 96 h, reaching a succinic acid yield of 0.66 ± 0.01 g/g and a sugar consumption of 96.64 ± 0.30%. Substrate inhibition was not observed in grape musts with 125-150 g/L initial sugars, provided that an adequate amount of yeast extract was available for bacteria. Alternative nitrogen sources to yeast extract (red wine lees, white wine lees, urea, NH4Cl, and choline chloride) were not suitable for A. succinogenes in grape must. KEY POINTS: • Vine shoots and surplus grape must were assessed for succinic acid bioproduction. • Succinic acid bioproduction was 21 g/L with vine shoots and 89 g/L with grape must. • Fermentation was efficient at high sugar loads if organic N supply was adequate.
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Application of solid-state fermentation by microbial biotechnology for bioprocessing of agro-industrial wastes from 1970 to 2020: A review and bibliometric analysis. Heliyon 2022; 8:e09173. [PMID: 35368548 PMCID: PMC8971590 DOI: 10.1016/j.heliyon.2022.e09173] [Citation(s) in RCA: 20] [Impact Index Per Article: 10.0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/16/2021] [Revised: 01/14/2022] [Accepted: 03/18/2022] [Indexed: 11/21/2022] Open
Abstract
This paper reviews the pertinent literature from 1970 to 2020 and presents a bibliometric analysis of research trends in the application of solid-state fermentation in the bioprocessing of agro-industrial wastes. A total 5630 publications of studies on solid-state fermentation that comprised of 5208 articles (92.50%), 340 book chapters (6.04%), 39 preprints (0.69%), 32 proceedings (0.56%), 8 edited books (0.14%) and 3 monographs (0.05%) were retrieved from Dimensions database. A review of the literature indicated that (i) fermentation of solid substrates is variously defined in the literature over the past 50 years, where "solid-state fermentation" is the most dominant research term used, and (ii) key products derived from the valorization of agro-industrial wastes through solid-state fermentation include, among others, enzymes, antioxidants, animal feed, biofuel, organic acids, biosurfactants, etc. Bibliometric analyses with VOSviewer revealed an astronomic increase in publications between 2000 and 2020, and further elucidated the most frequently explored core research topics, the most highly cited publications and authors, and countries/regions with the highest number of citations. The most cited publication between 2010 and 2020 had 382 citations compared to 725 citations for the most cited publication from 1970 to 2020. Ashok Pandey from India was the most published and cited author with 123 publications and 8,613 citations respectively; whereas Bioresource Technology was the most published and cited journal with 233 publications and 12,394 citations. Countries with the most publications and citations are Brazil, France, India, and Mexico. These findings suggest that research in the application of solid-state fermentation for bioprocessing of agro-industrial wastes has gained prominence over the past 50 years. Future perspectives and implications are discussed.
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Rozas S, Alomari N, Atilhan M, Aparicio S. Theoretical insights into the cineole-based deep eutectic solvents. J Chem Phys 2021; 154:184504. [PMID: 34241002 DOI: 10.1063/5.0048369] [Citation(s) in RCA: 6] [Impact Index Per Article: 2.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 02/02/2023] Open
Abstract
Deep eutectic solvents based on cineole as hydrogen bond acceptors and organic acids (succinic, malic, and lactic) as hydrogen bond donors are studied using a theoretical approach. The nature, strength, and extension of hydrogen bonding are analyzed, thus quantifying this prevailing interaction and its role in the fluid properties. Density functional theory was used to study small molecular clusters, and the topological characterization of the intermolecular forces was carried out using atoms in a molecule theory. Classical molecular dynamics simulations were considered to study nanoscopic bulk liquid properties and their relationship with relevant macroscopic properties such as density or thermal expansion. The reported results provide the characterization of environmentally friendly deep eutectic solvents and show the suitability of cineole for developing these sustainable materials.
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Affiliation(s)
- Sara Rozas
- Department of Chemistry, University of Burgos, 09001 Burgos, Spain
| | - Noor Alomari
- Department of Chemical and Paper Engineering, Western Michigan University, Kalamazoo, Michigan 49008, USA
| | - Mert Atilhan
- Department of Chemical and Paper Engineering, Western Michigan University, Kalamazoo, Michigan 49008, USA
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Gonzales TA, Carvalho Silvello MAD, Duarte ER, Santos LO, Alegre RM, Goldbeck R. Optimization of anaerobic fermentation of Actinobacillus succinogenes for increase the succinic acid production. BIOCATALYSIS AND AGRICULTURAL BIOTECHNOLOGY 2020. [DOI: 10.1016/j.bcab.2020.101718] [Citation(s) in RCA: 9] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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Dąbkowska K, Alvarado-Morales M, Kuglarz M, Angelidaki I. Miscanthus straw as substrate for biosuccinic acid production: Focusing on pretreatment and downstream processing. BIORESOURCE TECHNOLOGY 2019; 278:82-91. [PMID: 30684727 DOI: 10.1016/j.biortech.2019.01.051] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 10/31/2018] [Revised: 01/10/2019] [Accepted: 01/11/2019] [Indexed: 06/09/2023]
Abstract
The main aim of this study was to optimize pretreatment strategies of Miscanthus × giganteus for biosuccinic acid production. A successful pretreatment with organosolv method (80% w/w of glycerol, 1.25% of H2SO4), prevented sugars conversion to furfurals and organic acids, and thereby resulted in high sugar recovery (glucan > 98%, xylan > 91%) and biomass delignification (60%). Pretreated biomass was subjected to hydrolysis with various cellulolytic enzyme cocktails (Viscozyme® L, Carezyme 1000L®, β-Glucanase, Cellic® CTec2, Cellic® HTec2). The most effective enzymes mixture composed of Cellic® CTec2 (10% w/w), β-Glucanase (5% w/w) and Cellic® HTec2 (1% w/w) resulted in high glucose (93.1%) and xylose (69.2%) yields after glycerol-based pretreatment. Succinic acid yield of 75-82% was obtained after hydrolysates fermentation, using Actinobacillus succinogenes 130Z. Finally a successful downstream concept for succinic acid purification was proposed. The succinic acid recovery with high purity (>98%) was developed.
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Affiliation(s)
- Katarzyna Dąbkowska
- Faculty of Chemical and Process Engineering, Warsaw University of Technology, 00-645 Warsaw, Waryńskiego 1, Poland
| | - Merlin Alvarado-Morales
- Department of Environmental Engineering, Technical University of Denmark, Building 113, DK-2800 Lyngby, Denmark
| | - Mariusz Kuglarz
- Faculty of Materials, Civil and Environmental Engineering, University of Bielsko-Biala, Willowa 2, 43-309 Bielsko-Biala, Poland.
| | - Irini Angelidaki
- Department of Environmental Engineering, Technical University of Denmark, Building 113, DK-2800 Lyngby, Denmark
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Cao W, Wang Y, Luo J, Yin J, Xing J, Wan Y. Succinic acid biosynthesis from cane molasses under low pH by Actinobacillus succinogenes immobilized in luffa sponge matrices. BIORESOURCE TECHNOLOGY 2018; 268:45-51. [PMID: 30071412 DOI: 10.1016/j.biortech.2018.06.075] [Citation(s) in RCA: 27] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/23/2018] [Revised: 06/21/2018] [Accepted: 06/22/2018] [Indexed: 06/08/2023]
Abstract
Succinic acid (SA) production by Actinobacillus succinogenes 130Z using cane molasses as a low cost carbon source was developed. With molasses pretreated by 150 kDa membrane, the highest SA concentration (45.6 g/L), productivity (1.27 g/L·h) and yield (0.76 g SA/g sugars) were obtained under an optimal pH 6.4, which were increased by 1.04 folds compared to those with model sugar mixture due to the effect of vitamins in molasses. Meanwhile, the ratio of sugars in the cane molasses had little effect on SA production. To further enhance SA productivity, the cells were immobilized in luffa sponge matrices (LSM), and repeated batch cultures were carried out for 5 cycles, demonstrating a stable and reliable long-term performance. Compared with the batch culture, the SA productivity enhanced by 49.6% in the LSM system with repeated batch culture. These results suggest that the cell immobilization approach is promising for industrial applications.
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Affiliation(s)
- Weifeng Cao
- State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
| | - Yujue Wang
- State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; University of the Chinese Academy of Sciences, Chinese Academy of Sciences, Beijing 100049, China
| | - Jianquan Luo
- State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; University of the Chinese Academy of Sciences, Chinese Academy of Sciences, Beijing 100049, China
| | - Junxiang Yin
- China National Center for Biotechnology Development, Beijing 100036, China
| | - Jianmin Xing
- State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China
| | - Yinhua Wan
- State Key Laboratory of Biochemical Engineering, Institute of Process Engineering, Chinese Academy of Sciences, Beijing 100190, China; University of the Chinese Academy of Sciences, Chinese Academy of Sciences, Beijing 100049, China.
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Opportunities, challenges, and future perspectives of succinic acid production by Actinobacillus succinogenes. Appl Microbiol Biotechnol 2018; 102:9893-9910. [PMID: 30259101 DOI: 10.1007/s00253-018-9379-5] [Citation(s) in RCA: 43] [Impact Index Per Article: 7.2] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/21/2018] [Revised: 09/04/2018] [Accepted: 09/06/2018] [Indexed: 12/21/2022]
Abstract
Due to environmental issues and the depletion of fossil-based resources, ecofriendly sustainable biomass-based chemical production has been given more attention recently. Succinic acid (SA) is one of the top value added bio-based chemicals. It can be synthesized through microbial fermentation using various waste steam bioresources. Production of chemicals from waste streams has dual function as it alleviates environmental concerns; they could have caused because of their improper disposal and transform them into valuable products. To date, Actinobacillus succinogenes is termed as the best natural SA producer. However, few reviews regarding SA production by A. succinogenes were reported. Herewith, pathways and metabolic engineering strategies, biomass pretreatment and utilization, and process optimization related with SA fermentation by A. succinogenes were discussed in detail. In general, this review covered vital information including merits, achievements, progresses, challenges, and future perspectives in SA production using A. succinogenes. Therefore, it is believed that this review will provide platform to understand the potential of the strain and tackle existing hurdles so as to develop superior strain for industrial applications. It will also be used as a baseline for identification, isolation, and improvement of other SA-producing microbes.
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Continuous Succinic Acid Fermentation by Actinobacillus Succinogenes: Assessment of Growth and Succinic Acid Production Kinetics. Appl Biochem Biotechnol 2018; 187:782-799. [DOI: 10.1007/s12010-018-2846-8] [Citation(s) in RCA: 19] [Impact Index Per Article: 3.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 05/21/2018] [Accepted: 07/16/2018] [Indexed: 11/30/2022]
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Catalytic hydrogenation for a biomass-derived dicarboxylic acid valorisation with an ionic liquid and CO2 towards a perspective host guest building block molecule. J Supercrit Fluids 2018. [DOI: 10.1016/j.supflu.2017.05.032] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/19/2022]
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Ferone M, Raganati F, Olivieri G, Salatino P, Marzocchella A. Biosuccinic Acid from Lignocellulosic-Based Hexoses and Pentoses by Actinobacillus succinogenes: Characterization of the Conversion Process. Appl Biochem Biotechnol 2017; 183:1465-1477. [DOI: 10.1007/s12010-017-2514-4] [Citation(s) in RCA: 27] [Impact Index Per Article: 3.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/23/2017] [Accepted: 05/12/2017] [Indexed: 11/27/2022]
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Almqvist H, Pateraki C, Alexandri M, Koutinas A, Lidén G. Succinic acid production by Actinobacillus succinogenes from batch fermentation of mixed sugars. ACTA ACUST UNITED AC 2016; 43:1117-30. [DOI: 10.1007/s10295-016-1787-x] [Citation(s) in RCA: 24] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/04/2016] [Accepted: 05/21/2016] [Indexed: 10/21/2022]
Abstract
Abstract
Succinic acid production from the monosaccharides xylose, arabinose, glucose, mannose and galactose was studied using the bacterium Actinobacillus succinogenes. In Duran bottle cultures, containing 10 g/L of each of sugar, succinic acid was produced from all sugars except for galactose. The highest succinate yield, 0.56 g/g, was obtained with glucose, whereas the succinate yield was 0.42, 0.38 and 0.44 g/g for xylose, mannose and arabinose, respectively. The specific succinate productivity was 0.7 g/g h for glucose, but below 0.2 g/g h for the other sugars. Batch bioreactor fermentations were carried out using a sugar mixture of the five sugars giving a total concentration of 50 g/L, mimicking the distribution of sugars in spent sulfite liquor (SSL) from Eucalyptus which is rich in xylose. In this mixture, an almost complete conversion of all sugars (except galactose) was achieved resulting in a final succinate concentration of 21.8–26.8 g/L and a total yield of 0.59–0.68 g/g. There was evidence of co-consumption of glucose and xylose, whereas mannose was consumed after glucose. The main by-products were acetate 0.14–0.20 g/g and formate 0.08–0.13 g/g. NADH balance calculations suggested that NADH required for succinate production was not met solely from formate and acetate production, but other means of NADH production was necessary. Results from mixed sugar fermentations were verified using SSL as substrate resulting in a succinate yield of 0.60 g/g. In addition, it was found that CO2 sparging could replace carbonate supply in the form of MgCO3 without affecting the succinate yield.
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Affiliation(s)
- Henrik Almqvist
- grid.4514.4 0000000109302361 Department of Chemical Engineering Lund University P.O. Box 124 221 00 Lund Sweden
| | - Chrysanthi Pateraki
- grid.10985.35 0000000107941186 Department of Food Science and Human Nutrition Agricultural University of Athens Iera Odos 75 118 55 Athens Greece
| | - Maria Alexandri
- grid.10985.35 0000000107941186 Department of Food Science and Human Nutrition Agricultural University of Athens Iera Odos 75 118 55 Athens Greece
| | - Apostolis Koutinas
- grid.10985.35 0000000107941186 Department of Food Science and Human Nutrition Agricultural University of Athens Iera Odos 75 118 55 Athens Greece
| | - Gunnar Lidén
- grid.4514.4 0000000109302361 Department of Chemical Engineering Lund University P.O. Box 124 221 00 Lund Sweden
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Sadhukhan S, Villa R, Sarkar U. Microbial production of succinic acid using crude and purified glycerol from a Crotalaria juncea based biorefinery. BIOTECHNOLOGY REPORTS (AMSTERDAM, NETHERLANDS) 2016; 10:84-93. [PMID: 28352528 PMCID: PMC5040874 DOI: 10.1016/j.btre.2016.03.008] [Citation(s) in RCA: 25] [Impact Index Per Article: 3.1] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Subscribe] [Scholar Register] [Received: 11/12/2015] [Revised: 02/08/2016] [Accepted: 03/31/2016] [Indexed: 11/23/2022]
Abstract
Microbial conversion of crude and purified glycerol obtained in the process of biorefining Crotalaria juncea is carried out to produce succinic acid using Escherichia coli. Batch tests are performed for nine different substrate concentrations of commercial, purified and crude glycerol, in order to observe cell growth and substrate utilization rate. Inhibitory (Halden-Andrew, Aiba-Edward, Tessier type and Andrews) as well as non-inhibitory (Monod, Moser and Tessier) models are fitted to the relationship between specific growth rate and substrate concentration obtained from the growth curves. Considering the inhibition effect, Aiba-Edward model ranked 1 out of 7 in case of two samples and Haldane-Andrew model ranked 1 in case of one sample. Aiba-Edward model gave the best fitment for a large range of concentrations of all the three types of glycerol, crude, purified and laboratory grade. Maximum production of succinic acid is obtained from commercial glycerol at pH 7 and 37.5 °C.
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Affiliation(s)
- Suvra Sadhukhan
- Department of Chemical Engineering, Jadavpur University, Kolkata 700032, India
| | - Raffaella Villa
- School of Energy, Environment and Agrifood, Cranfield University, Beds MK43 0AL, United Kingdom
| | - Ujjaini Sarkar
- Department of Chemical Engineering, Jadavpur University, Kolkata 700032, India
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Kuglarz M, Alvarado-Morales M, Karakashev D, Angelidaki I. Integrated production of cellulosic bioethanol and succinic acid from industrial hemp in a biorefinery concept. BIORESOURCE TECHNOLOGY 2016; 200:639-47. [PMID: 26551652 DOI: 10.1016/j.biortech.2015.10.081] [Citation(s) in RCA: 11] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/11/2015] [Revised: 10/20/2015] [Accepted: 10/23/2015] [Indexed: 05/03/2023]
Abstract
The aim of this study was to develop integrated biofuel (cellulosic bioethanol) and biochemical (succinic acid) production from industrial hemp (Cannabis sativa L.) in a biorefinery concept. Two types of pretreatments were studied (dilute-acid and alkaline oxidative method). High cellulose recovery (>95%) as well as significant hemicelluloses solubilization (49-59%) after acid-based method and lignin solubilization (35-41%) after alkaline H2O2 method were registered. Alkaline pretreatment showed to be superior over the acid-based method with respect to the rate of enzymatic hydrolysis and ethanol productivity. With respect to succinic acid production, the highest productivity was obtained after liquid fraction fermentation originated from steam treatment with 1.5% of acid. The mass balance calculations clearly showed that 149kg of EtOH and 115kg of succinic acid can be obtained per 1ton of dry hemp. Results obtained in this study clearly document the potential of industrial hemp for a biorefinery.
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Affiliation(s)
- Mariusz Kuglarz
- Faculty of Materials, Civil and Environmental Engineering, University of Bielsko-Biala, Willowa 2, 43-309 Bielsko-Biala, Poland
| | - Merlin Alvarado-Morales
- Department of Environmental Engineering, Technical University of Denmark, DK-2800 Kongens Lyngby, Denmark
| | - Dimitar Karakashev
- Department of Environmental Engineering, Technical University of Denmark, DK-2800 Kongens Lyngby, Denmark
| | - Irini Angelidaki
- Department of Environmental Engineering, Technical University of Denmark, DK-2800 Kongens Lyngby, Denmark.
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Surendra K, Sawatdeenarunat C, Shrestha S, Sung S, Khanal SK. Anaerobic Digestion-Based Biorefinery for Bioenergy and Biobased Products. Ind Biotechnol (New Rochelle N Y) 2015. [DOI: 10.1089/ind.2015.0001] [Citation(s) in RCA: 44] [Impact Index Per Article: 4.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/13/2022] Open
Affiliation(s)
- K.C. Surendra
- Department of Molecular Biosciences and Bioengineering, University of Hawai'i at Mānoa, Honolulu, HI
| | - Chayanon Sawatdeenarunat
- Department of Molecular Biosciences and Bioengineering, University of Hawai'i at Mānoa, Honolulu, HI
| | - Shilva Shrestha
- Department of Molecular Biosciences and Bioengineering, University of Hawai'i at Mānoa, Honolulu, HI
| | - Shihwu Sung
- College of Agriculture, Forestry and Natural Resource Management, University of Hawai'i at Hilo, Hilo, HI
| | - Samir Kumar Khanal
- Department of Molecular Biosciences and Bioengineering, University of Hawai'i at Mānoa, Honolulu, HI
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Gunnarsson IB, Kuglarz M, Karakashev D, Angelidaki I. Thermochemical pretreatments for enhancing succinic acid production from industrial hemp (Cannabis sativa L.). BIORESOURCE TECHNOLOGY 2015; 182:58-66. [PMID: 25682224 DOI: 10.1016/j.biortech.2015.01.126] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.6] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/17/2014] [Revised: 01/26/2015] [Accepted: 01/28/2015] [Indexed: 05/03/2023]
Abstract
The aim of this study was to develop an efficient thermochemical method for treatment of industrial hemp biomass, in order to increase its bioconversion to succinic acid. Industrial hemp was subjected to various thermochemical pretreatments using 0-3% H2SO4, NaOH or H2O2 at 121-180°C prior to enzymatic hydrolysis. The influence of the different pretreatments on hydrolysis and succinic acid production by Actinobacillus succinogenes 130Z was investigated in batch mode, using anaerobic bottles and bioreactors. Enzymatic hydrolysis and fermentation of hemp material pretreated with 3% H2O2 resulted in the highest overall sugar yield (73.5%), maximum succinic acid titer (21.9 g L(-1)), as well as the highest succinic acid yield (83%). Results obtained clearly demonstrated the impact of different pretreatments on the bioconversion efficiency of industrial hemp into succinic acid.
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Affiliation(s)
- Ingólfur B Gunnarsson
- Department of Environmental Engineering, Technical University of Denmark, Building 115, DK-2800 Lyngby, Denmark
| | - Mariusz Kuglarz
- Faculty of Materials and Environmental Sciences, University of Bielsko-Biala, Willowa 2, Bielsko-Biala, Poland
| | - Dimitar Karakashev
- Department of Environmental Engineering, Technical University of Denmark, Building 115, DK-2800 Lyngby, Denmark
| | - Irini Angelidaki
- Department of Environmental Engineering, Technical University of Denmark, Building 115, DK-2800 Lyngby, Denmark.
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Bradfield MFA, Mohagheghi A, Salvachúa D, Smith H, Black BA, Dowe N, Beckham GT, Nicol W. Continuous succinic acid production by Actinobacillus succinogenes on xylose-enriched hydrolysate. BIOTECHNOLOGY FOR BIOFUELS 2015; 8:181. [PMID: 26581168 PMCID: PMC4650334 DOI: 10.1186/s13068-015-0363-3] [Citation(s) in RCA: 59] [Impact Index Per Article: 6.6] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 08/11/2015] [Accepted: 10/22/2015] [Indexed: 05/02/2023]
Abstract
BACKGROUND Bio-manufacturing of high-value chemicals in parallel to renewable biofuels has the potential to dramatically improve the overall economic landscape of integrated lignocellulosic biorefineries. However, this will require the generation of carbohydrate streams from lignocellulose in a form suitable for efficient microbial conversion and downstream processing appropriate to the desired end use, making overall process development, along with selection of appropriate target molecules, crucial to the integrated biorefinery. Succinic acid (SA), a high-value target molecule, can be biologically produced from sugars and has the potential to serve as a platform chemical for various chemical and polymer applications. However, the feasibility of microbial SA production at industrially relevant productivities and yields from lignocellulosic biorefinery streams has not yet been reported. RESULTS Actinobacillus succinogenes 130Z was immobilised in a custom continuous fermentation setup to produce SA on the xylose-enriched fraction of a non-detoxified, xylose-rich corn stover hydrolysate stream produced from deacetylation and dilute acid pretreatment. Effective biofilm attachment, which serves as a natural cell retention strategy to increase cell densities, productivities and resistance to toxicity, was accomplished by means of a novel agitator fitting. A maximum SA titre, yield and productivity of 39.6 g L(-1), 0.78 g g(-1) and 1.77 g L(-1) h(-1) were achieved, respectively. Steady states were obtained at dilution rates of 0.02, 0.03, 0.04, and 0.05 h(-1) and the stirred biofilm reactor was stable over prolonged periods of operation with a combined fermentation time of 1550 h. Furthermore, it was found that a gradual increase in the dilution rate was required to facilitate adaptation of the culture to the hydrolysate, suggesting a strong evolutionary response to the toxic compounds in the hydrolysate. Moreover, the two primary suspected fermentation inhibitors, furfural and HMF, were metabolised during fermentation with the concentration of each remaining at zero across all steady states. CONCLUSIONS The results demonstrate that immobilised A. succinogenes has the potential for effective conversion of an industrially relevant, biomass-derived feed stream to succinic acid. Furthermore, due to the attractive yields, productivities and titres achieved in this study, the process has the potential to serve as a means for value-added chemical manufacturing in the integrated biorefinery.
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Affiliation(s)
- Michael F. A. Bradfield
- />Department of Chemical Engineering, University of Pretoria, Lynnwood Road, Hatfield, Pretoria, 0002 South Africa
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Ali Mohagheghi
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Davinia Salvachúa
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Holly Smith
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Brenna A. Black
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Nancy Dowe
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Gregg T. Beckham
- />National Renewable Energy Laboratory, National Bioenergy Center, 15013 Denver West Parkway, Golden, CO 80401 USA
| | - Willie Nicol
- />Department of Chemical Engineering, University of Pretoria, Lynnwood Road, Hatfield, Pretoria, 0002 South Africa
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Tippkötter N, Duwe AM, Wiesen S, Sieker T, Ulber R. Enzymatic hydrolysis of beech wood lignocellulose at high solid contents and its utilization as substrate for the production of biobutanol and dicarboxylic acids. BIORESOURCE TECHNOLOGY 2014; 167:447-55. [PMID: 25006020 DOI: 10.1016/j.biortech.2014.06.052] [Citation(s) in RCA: 28] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 03/05/2014] [Revised: 06/05/2014] [Accepted: 06/06/2014] [Indexed: 05/12/2023]
Abstract
The development of a cost-effective hydrolysis for crude cellulose is an essential part of biorefinery developments. To establish such high solid hydrolysis, a new solid state reactor with static mixing is used. However, concentrations >10% (w/w) cause a rate and yield reduction of enzymatic hydrolysis. By optimizing the synergetic activity of cellulolytic enzymes at solid concentrations of 9%, 17% and 23% (w/w) of crude Organosolv cellulose, glucose concentrations of 57, 113 and 152 g L(-1) are reached. However, the glucose yield decreases from 0.81 to 0.72 g g(-1) at 17% (w/w). Optimal conditions for hydrolysis scale-up under minimal enzyme addition are identified. As result, at 23% (w/w) crude cellulose the glucose yield increases from 0.29 to 0.49 g g(-1). As proof of its applicability, biobutanol, succinic and itaconic acid are produced with the crude hydrolysate. The potential of the substrate is proven e.g. by a high butanol yield of 0.33 g g(-1).
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Affiliation(s)
- Nils Tippkötter
- University of Kaiserslautern, Institute of Bioprocess Engineering, Kaiserslautern, Germany
| | - Anna-Maria Duwe
- University of Kaiserslautern, Institute of Bioprocess Engineering, Kaiserslautern, Germany
| | - Sebastian Wiesen
- University of Kaiserslautern, Institute of Bioprocess Engineering, Kaiserslautern, Germany
| | - Tim Sieker
- University of Kaiserslautern, Institute of Bioprocess Engineering, Kaiserslautern, Germany
| | - Roland Ulber
- University of Kaiserslautern, Institute of Bioprocess Engineering, Kaiserslautern, Germany.
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Mixed Food Waste as Renewable Feedstock in Succinic Acid Fermentation. Appl Biochem Biotechnol 2014; 174:1822-33. [DOI: 10.1007/s12010-014-1169-7] [Citation(s) in RCA: 45] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 05/04/2014] [Accepted: 08/15/2014] [Indexed: 10/24/2022]
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Succinic acid production with Actinobacillus succinogenes: rate and yield analysis of chemostat and biofilm cultures. Microb Cell Fact 2014. [PMID: 25259880 DOI: 10.1186/s12934-014-0111-6.] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Abstract] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022] Open
Abstract
BACKGROUND Succinic acid is well established as bio-based platform chemical with production quantities expecting to increase exponentially within the next decade. Actinobacillus succinogenes is by far the most studied wild organism for producing succinic acid and is known for high yield and titre during production on various sugars in batch culture. At low shear conditions continuous fermentation with A. succinogenes results in biofilm formation. In this study, a novel shear controlled fermenter was developed that enabled: 1) chemostat operation where self-immobilisation was opposed by high shear rates and, 2) in-situ removal of biofilm by increasing shear rates and subsequent analysis thereof. RESULTS The volumetric productivity of the biofilm fermentations were an order of magnitude more than the chemostat runs. In addition the biofilm runs obtained substantially higher yields. Succinic acid to acetic acid ratios for chemostat runs were 1.28±0.2 g.g(-1), while the ratios for biofilm runs started at 2.4 g.g(-1) and increased up to 3.3 g.g(-1) as glucose consumption increased. This corresponded to an overall yield on glucose of 0.48±0.05 g.g(-1) for chemostat runs, while the yields varied between 0.63 g.g(-1) and 0.74 g.g(-1) for biofilm runs. Specific growth rates (μ) were shown to be severely inhibited by the formation of organic acids, with μ only 12% of μ(max) at a succinic acid titre of 7 g.L(-1). Maintenance production of succinic acid was shown to be dominant for the biofilm runs with cell based production rates (extracellular polymeric substance removed) decreasing as SA titre increases. CONCLUSIONS The novel fermenter allowed for an in-depth bioreaction analysis of A. succinogenes. Biofilm cells achieve higher SA yields than suspended cells and allow for operation at higher succinic acid titre. Both growth and maintenance rates were shown to drastically decrease with succinic acid titre. The A. succinogenes biofilm process has vast potential, where self-induced high cell densities result in higher succinic acid productivity and yield.
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Succinic acid production with Actinobacillus succinogenes: rate and yield analysis of chemostat and biofilm cultures. Microb Cell Fact 2014; 13:111. [PMID: 25259880 PMCID: PMC4154526 DOI: 10.1186/s12934-014-0111-6] [Citation(s) in RCA: 48] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/15/2014] [Accepted: 07/23/2014] [Indexed: 01/11/2023] Open
Abstract
Background Succinic acid is well established as bio-based platform chemical with production quantities expecting to increase exponentially within the next decade. Actinobacillus succinogenes is by far the most studied wild organism for producing succinic acid and is known for high yield and titre during production on various sugars in batch culture. At low shear conditions continuous fermentation with A. succinogenes results in biofilm formation. In this study, a novel shear controlled fermenter was developed that enabled: 1) chemostat operation where self-immobilisation was opposed by high shear rates and, 2) in-situ removal of biofilm by increasing shear rates and subsequent analysis thereof. Results The volumetric productivity of the biofilm fermentations were an order of magnitude more than the chemostat runs. In addition the biofilm runs obtained substantially higher yields. Succinic acid to acetic acid ratios for chemostat runs were 1.28±0.2 g.g-1, while the ratios for biofilm runs started at 2.4 g.g-1 and increased up to 3.3 g.g-1 as glucose consumption increased. This corresponded to an overall yield on glucose of 0.48±0.05 g.g-1 for chemostat runs, while the yields varied between 0.63 g.g-1 and 0.74 g.g-1 for biofilm runs. Specific growth rates (μ) were shown to be severely inhibited by the formation of organic acids, with μ only 12% of μmax at a succinic acid titre of 7 g.L-1. Maintenance production of succinic acid was shown to be dominant for the biofilm runs with cell based production rates (extracellular polymeric substance removed) decreasing as SA titre increases. Conclusions The novel fermenter allowed for an in-depth bioreaction analysis of A. succinogenes. Biofilm cells achieve higher SA yields than suspended cells and allow for operation at higher succinic acid titre. Both growth and maintenance rates were shown to drastically decrease with succinic acid titre. The A. succinogenes biofilm process has vast potential, where self-induced high cell densities result in higher succinic acid productivity and yield.
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Carlescu A, Blaga AC, Galaction AI, Turnea M, Caşcaval D. Interfacial Mass Transfer in the Reactive Extraction Process of Succinic Acid from Viscous Aqueous Solutions. SEP SCI TECHNOL 2014. [DOI: 10.1080/01496395.2013.868488] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 10/25/2022]
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Lapkin A, Adou E, Mlambo BN, Chemat S, Suberu J, Collis AE, Clark A, Barker G. Integrating medicinal plants extraction into a high-value biorefinery: An example of Artemisia annua L. CR CHIM 2014. [DOI: 10.1016/j.crci.2013.10.023] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 01/16/2023]
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Sun WJ, Yun QQ, Zhou YZ, Cui FJ, Yu SL, Zhou Q, Sun L. Continuous 2-keto-gluconic acid (2KGA) production from corn starch hydrolysate by Pseudomonas fluorescens AR4. Biochem Eng J 2013. [DOI: 10.1016/j.bej.2013.05.010] [Citation(s) in RCA: 14] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/26/2022]
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Caşcaval D, Cârlescu A, Galaction AI, Turnea M. Study on Biomass Impact on the Reactive Extraction of Succinic Acid from Actinobacillus succinogenes Suspensions. Ind Eng Chem Res 2013. [DOI: 10.1021/ie4016792] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Affiliation(s)
- Dan Caşcaval
- Department of Biochemical Engineering, Faculty of Chemical Engineering and Environmental Protection, ″Gheorghe Asachi″ Technical University of Iasi, D. Mangeron 73, 700050 Iasi, Romania
| | - Alexandra Cârlescu
- Department of Biochemical Engineering, Faculty of Chemical Engineering and Environmental Protection, ″Gheorghe Asachi″ Technical University of Iasi, D. Mangeron 73, 700050 Iasi, Romania
| | - Anca-Irina Galaction
- Department of Biomedical
Science, Faculty of Medical Bioengineering, “Gr.T. Popa” University of Medicine and Pharmacy of Iasi, M. Kogalniceanu 9-13, 700454 Iasi, Romania
| | - Marius Turnea
- Department of Biomedical
Science, Faculty of Medical Bioengineering, “Gr.T. Popa” University of Medicine and Pharmacy of Iasi, M. Kogalniceanu 9-13, 700454 Iasi, Romania
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Ultrasonic pretreatment and acid hydrolysis of sugarcane bagasse for succinic acid production using Actinobacillus succinogenes. Bioprocess Biosyst Eng 2013; 36:1779-85. [DOI: 10.1007/s00449-013-0953-z] [Citation(s) in RCA: 45] [Impact Index Per Article: 4.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 01/15/2013] [Accepted: 04/11/2013] [Indexed: 10/26/2022]
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Kloetzer L, Caşcaval D, Galaction AI. INFLUENCE OF SOLVENT POLARITY ON INTERFACIAL MECHANISM AND EFFICIENCY OF SUCCINIC ACID REACTIVE EXTRACTION WITH TRI-n-OCTYLAMINE. CHEM ENG COMMUN 2013. [DOI: 10.1080/00986445.2012.717319] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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28
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Galaction AI, Poştaru M, Caşcaval D, Kloetzer L. Selective Separation of Carboxylic Acids Obtained by Succinic Acid Fermentation Using Facilitated Pertraction. SOLVENT EXTRACTION AND ION EXCHANGE 2013. [DOI: 10.1080/07366299.2012.735520] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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29
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Zhou X, Zheng P. Spirit-based distillers’ grain as a promising raw material for succinic acid production. Biotechnol Lett 2013; 35:679-84. [DOI: 10.1007/s10529-013-1147-0] [Citation(s) in RCA: 21] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/19/2012] [Accepted: 01/14/2013] [Indexed: 10/27/2022]
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Caşcaval D, Kloetzer L, Galaction AI, Vlysidis A, Webb C. Fractionation of Carboxylic Acids Mixture Obtained by Succinic Fermentation using Reactive Extraction. SEP SCI TECHNOL 2013. [DOI: 10.1080/01496395.2012.691593] [Citation(s) in RCA: 8] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 10/27/2022]
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31
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Actinobacillus succinogenes ATCC 55618 fermentation medium optimization for the production of succinic acid by response surface methodology. J Biomed Biotechnol 2012; 2012:626137. [PMID: 23093852 PMCID: PMC3470900 DOI: 10.1155/2012/626137] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 03/31/2012] [Revised: 05/29/2012] [Accepted: 06/08/2012] [Indexed: 11/23/2022] Open
Abstract
As a potential intermediary feedstock, succinic acid takes an important place in bulk chemical productions. For the first time, a method combining Plackett-Burman design (PBD), steepest ascent method (SA), and Box-Behnken design (BBD) was developed to optimize Actinobacillus succinogenes ATCC 55618 fermentation medium. First, glucose, yeast extract, and MgCO3 were identified to be key medium components by PBD. Second, preliminary optimization was run by SA method to access the optimal region of the key medium components. Finally, the responses, that is, the production of succinic acid, were optimized simultaneously by using BBD, and the optimal concentration was located to be 84.6 g L−1 of glucose, 14.5 g L−1 of yeast extract, and 64.7 g L−1 of MgCO3. Verification experiment indicated that the maximal succinic acid production of 52.7 ± 0.8 g L−1 was obtained under the identified optimal conditions. The result agreed with the predicted value well. Compared with that of the basic medium, the production of succinic acid and yield of succinic acid against glucose were enhanced by 67.3% and 111.1%, respectively. The results obtained in this study may be useful for the industrial commercial production of succinic acid.
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Caşcaval D, Poştaru M, Galaction AI, Kloetzer L. Comparitive study on facilitated pertraction of succinic acid using TRI-n-octylamine without and with 1-octanol. CAN J CHEM ENG 2012. [DOI: 10.1002/cjce.21730] [Citation(s) in RCA: 2] [Impact Index Per Article: 0.2] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/06/2022]
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33
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Catalytic Transformations of Biomass-Derived Materials into Value-Added Chemicals. CATALYSIS SURVEYS FROM ASIA 2012. [DOI: 10.1007/s10563-012-9142-3] [Citation(s) in RCA: 84] [Impact Index Per Article: 7.0] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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Abstract
In the current climate of several interrelated impending global crises, namely, climate change, chemicals, energy, and oil, the impact of green chemistry with respect to chemicals and biofuels generated from within a holistic concept of a biorefinery is discussed. Green chemistry provides unique opportunities for innovation via product substitution, new feedstock generation, catalysis in aqueous media, utilization of microwaves, and scope for alternative or natural solvents. The potential of utilizing waste as a new resource and the development of integrated facilities producing multiple products from biomass is discussed under the guise of biorefineries. Biofuels are discussed in depth, as they not only provide fuel (energy) but are also a source of feedstock chemicals. In the future, the commercial success of biofuels commensurate with consumer demand will depend on the availability of new green (bio)chemical technologies capable of converting waste biomass to fuel in a context of a biorefinery.
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Affiliation(s)
- James H Clark
- Department of Chemistry, University of York, Heslington, York, UK.
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35
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Hong UG, Park HW, Lee J, Hwang S, Song IK. Hydrogenation of succinic acid to γ-butyrolactone (GBL) over ruthenium catalyst supported on surfactant-templated mesoporous carbon. J IND ENG CHEM 2012. [DOI: 10.1016/j.jiec.2011.11.054] [Citation(s) in RCA: 27] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/17/2022]
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36
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Chen KQ, Li J, Ma JF, Jiang M, Wei P, Liu ZM, Ying HJ. Succinic acid production by Actinobacillus succinogenes using hydrolysates of spent yeast cells and corn fiber. BIORESOURCE TECHNOLOGY 2011; 102:1704-8. [PMID: 20801644 DOI: 10.1016/j.biortech.2010.08.011] [Citation(s) in RCA: 59] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 04/14/2010] [Revised: 08/02/2010] [Accepted: 08/04/2010] [Indexed: 05/03/2023]
Abstract
The enzymatic hydrolysate of spent yeast cells was evaluated as a nitrogen source for succinic acid production by Actinobacillus succinogenes NJ113, using corn fiber hydrolysate as a carbon source. When spent yeast cell hydrolysate was used directly as a nitrogen source, a maximum succinic acid concentration of 35.5 g/l was obtained from a glucose concentration of 50 g/l, with a glucose utilization of 95.2%. Supplementation with individual vitamins showed that biotin was the most likely factor to be limiting for succinic acid production with spent yeast cell hydrolysate. After supplementing spent yeast cell hydrolysate and 90 g/l of glucose with 150 μg/l of biotin, cell growth increased 32.5%, glucose utilization increased 37.6%, and succinic acid concentration was enhanced 49.0%. As a result, when biotin-supplemented spent yeast cell hydrolysate was used with corn fiber hydrolysate, a succinic acid yield of 67.7% was obtained from 70.3 g/l of total sugar concentration, with a productivity of 0.63 g/(l h). Our results suggest that biotin-supplemented spent yeast cell hydrolysate may be an alternative nitrogen source for the efficient production of succinic acid by A. succinogenes NJ113, using renewable resources.
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Affiliation(s)
- Ke-Quan Chen
- State Key Laboratory of Materials-Oriented Chemical Engineering, College of Biotechnology and Pharmaceutical Engineering, Nanjing University of Technology, Nanjing 210009, People's Republic of China
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Chen K, Zhang H, Miao Y, Wei P, Chen J. Simultaneous saccharification and fermentation of acid-pretreated rapeseed meal for succinic acid production using Actinobacillus succinogenes. Enzyme Microb Technol 2010; 48:339-44. [PMID: 22112947 DOI: 10.1016/j.enzmictec.2010.12.009] [Citation(s) in RCA: 61] [Impact Index Per Article: 4.4] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/06/2010] [Revised: 12/15/2010] [Accepted: 12/16/2010] [Indexed: 10/18/2022]
Abstract
Rapeseed meal was evaluated for succinic acid production by simultaneous saccharification and fermentation using Actinobacillus succinogenes ATCC 55618. Diluted sulfuric acid pretreatment and subsequent hydrolysis with pectinase was used to release sugars from rapeseed meal. The effects of culture pH, pectinase loading and yeast extract concentration on succinic acid production were investigated. When simultaneous saccharification and fermentation of diluted acid pretreated rapeseed meal with a dry matter content of 12.5% (w/v) was performed at pH 6.4 and a pectinase loading of 2% (w/w, on dry matter) without supplementation of yeast extract, a succinic acid concentration of 15.5 g/L was obtained at a yield of 12.4 g/100g dry matter. Fed-batch simultaneous saccharification and fermentation was carried out with supplementation of concentrated pretreated rapeseed meal and pectinase at 18 and 28 h to yield a final dry matter content of 20.5% and pectinase loading of 2%, with the succinic acid concentration enhanced to 23.4 g/L at a yield of 11.5 g/100g dry matter and a productivity of 0.33 g/(Lh). This study suggests that rapeseed meal may be an alternative substrate for the efficient production of succinic acid by A. succinogenes without requiring nitrogen source supplementation.
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Affiliation(s)
- Kequan Chen
- Faculty of Bioresource Sciences, Akita Prefectural University, Kaidobata-Nishi 241-438, Shimoshinjo-Nakano, Akita-shi, Akita 010-0195, Japan
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Xu J, Guo BH. Microbial Succinic Acid, Its Polymer Poly(butylene succinate), and Applications. MICROBIOLOGY MONOGRAPHS 2010. [DOI: 10.1007/978-3-642-03287-5_14] [Citation(s) in RCA: 60] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 01/04/2023]
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40
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Dorado MP, Lin SKC, Koutinas A, Du C, Wang R, Webb C. Cereal-based biorefinery development: Utilisation of wheat milling by-products for the production of succinic acid. J Biotechnol 2009; 143:51-9. [DOI: 10.1016/j.jbiotec.2009.06.009] [Citation(s) in RCA: 67] [Impact Index Per Article: 4.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/25/2008] [Revised: 04/11/2009] [Accepted: 06/05/2009] [Indexed: 10/20/2022]
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41
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Octave S, Thomas D. Biorefinery: Toward an industrial metabolism. Biochimie 2009; 91:659-64. [DOI: 10.1016/j.biochi.2009.03.015] [Citation(s) in RCA: 128] [Impact Index Per Article: 8.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 12/15/2008] [Accepted: 03/20/2009] [Indexed: 10/21/2022]
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42
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Jiang M, Chen K, Liu Z, Wei P, Ying H, Chang H. Succinic acid production by Actinobacillus succinogenes using spent brewer's yeast hydrolysate as a nitrogen source. Appl Biochem Biotechnol 2009; 160:244-54. [PMID: 19418259 DOI: 10.1007/s12010-009-8649-1] [Citation(s) in RCA: 20] [Impact Index Per Article: 1.3] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/10/2008] [Accepted: 04/14/2009] [Indexed: 10/20/2022]
Abstract
To develop a cost-effective fermentation medium, spent brewer's yeast hydrolysate was evaluated as a nitrogen source for succinic acid production by Actinobacillus succinogenes NJ113 in glucose-containing media. Autolysis and enzymatic hydrolysis were used to hydrolyze the spent brewer's yeast cells to release the nutrients. The results showed that enzymatic hydrolysis was a more effective method due to the higher succinic acid yield and cell growth. However, the incomplete glucose consumption indicated existence of nutrient limitation. Vitamins were subsequently identified as the main limiting factors for succinic acid production using enzymatically hydrolyzed spent brewer's yeast as a nitrogen source. After the addition of vitamins, cell growth and succinic acid concentration both improved. As a result, 15 g/L yeast extract could be successfully replaced with the enzymatic hydrolysate of spent brewer's yeast with vitamins supplementation, resulting in a production of 46.8 g/L succinic acid from 68 g/L glucose.
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Affiliation(s)
- Min Jiang
- State Key Laboratory of Materials-Oriented Chemical Engineering, College of Life Science and Pharmacy, Nanjing University of Technology, Nanjing, People's Republic of China.
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Wang R, Godoy LC, Shaarani SM, Melikoglu M, Koutinas A, Webb C. Improving wheat flour hydrolysis by an enzyme mixture from solid state fungal fermentation. Enzyme Microb Technol 2009. [DOI: 10.1016/j.enzmictec.2008.10.002] [Citation(s) in RCA: 41] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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44
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Zheng P, Dong JJ, Sun ZH, Ni Y, Fang L. Fermentative production of succinic acid from straw hydrolysate by Actinobacillus succinogenes. BIORESOURCE TECHNOLOGY 2009; 100:2425-9. [PMID: 19128958 DOI: 10.1016/j.biortech.2008.11.043] [Citation(s) in RCA: 103] [Impact Index Per Article: 6.9] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 09/05/2008] [Revised: 11/24/2008] [Accepted: 11/26/2008] [Indexed: 05/02/2023]
Abstract
In this work, straw hydrolysates were used to produce succinic acid by Actinobacillus succinogenes CGMCC1593 for the first time. Results indicated that both glucose and xylose in the straw hydrolysates were utilized in succinic acid production, and the hydrolysates of corn straw was better than that of rice or wheat straw in anaerobic fermentation of succinic acid. However, cell growth and succinic acid production were inhibited when the initial concentration of sugar, which was from corn straw hydrolysate (CSH), was higher than 60 g l(-1). In batch fermentation, 45.5 g l(-1) succinic acid concentration and 80.7% yield were attained after 48 h incubation with 58 g l(-1) of initial sugar from corn straw hydrolysate in a 5-l stirred bioreactor. While in fed-batch fermentation, concentration of succinic acid achieved 53.2 g l(-1) at a rate of 1.21 g l(-1) h(-1) after 44 h of fermentation. Our work suggested that corn straw could be utilized for the economical production of succinic acid by A. succinogenes.
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Affiliation(s)
- Pu Zheng
- The Key Laboratory of Industrial Biotechnology, Ministry of Education, School of Biotechnology, Jiangnan University, Wuxi, Jiangsu Province 214122, PR China
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Du C, Lin SKC, Koutinas A, Wang R, Dorado P, Webb C. A wheat biorefining strategy based on solid-state fermentation for fermentative production of succinic acid. BIORESOURCE TECHNOLOGY 2008; 99:8310-5. [PMID: 18434138 DOI: 10.1016/j.biortech.2008.03.019] [Citation(s) in RCA: 53] [Impact Index Per Article: 3.3] [Reference Citation Analysis] [Abstract] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 11/15/2007] [Revised: 02/28/2008] [Accepted: 03/01/2008] [Indexed: 05/03/2023]
Abstract
In this study, a novel generic feedstock production strategy based on solid-state fermentation (SSF) has been developed and applied to the fermentative production of succinic acid. Wheat was fractionated into bran, gluten and gluten-free flour by milling and gluten extraction processes. The bran, which would normally be a waste product of the wheat milling industry, was used to produce glucoamylase and protease enzymes via SSF using Aspergillus awamori and Aspergillus oryzae, respectively. The resulting solutions were separately utilised for the hydrolysis of gluten-free flour and gluten to generate a glucose-rich stream of over 140gl(-1) glucose and a nitrogen-rich stream of more than 3.5gl(-1) free amino nitrogen. A microbial feedstock consisting of these two streams contained all the essential nutrients required for succinic acid fermentations using Actinobacillus succinogenes. In a fermentation using only the combined hydrolysate streams, around 22gl(-1) succinic acid was produced. The addition of MgCO3 into the wheat-derived medium improved the succinic acid production further to more than 64gl(-1). These results demonstrate the SSF-based strategy is a successful approach for the production of a generic feedstock from wheat, and that this feedstock can be efficiently utilised for succinic acid production.
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Affiliation(s)
- Chenyu Du
- Satake Centre for Grain Process Engineering, School of Chemical Engineering and Analytical Science, University of Manchester, P.O. Box 88, Manchester M60 1QD, United Kingdom
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Substrate and product inhibition kinetics in succinic acid production by Actinobacillus succinogenes. Biochem Eng J 2008. [DOI: 10.1016/j.bej.2008.03.013] [Citation(s) in RCA: 148] [Impact Index Per Article: 9.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
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Tokiwa Y, Calabia BP. Biological production of functional chemicals from renewable resources. CAN J CHEM 2008. [DOI: 10.1139/v08-046] [Citation(s) in RCA: 34] [Impact Index Per Article: 2.1] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/22/2022]
Abstract
The development and implementation of renewable feedstocks for the production of multifunctional chemicals has received attention from the food and pharmaceutical industries and also as potential raw materials for the manufacture of biodegradable polymers. A major shift towards renewable resources, however, requires new ways to optimize and evaluate industrial processes. There are several possibilities to replace chemical techniques with biological methods based on renewable resources. This review discusses some examples of process development in which a biotechnological route might be favorable leading to industrial realization. Herein are described the production of biomaterials that can be used as monomers in plastics, such as lactic acid for polylactide (PLA), (R)-3-hydroxybutyric acid (R-3HB) for poly[(R)-3-hydroxybutyrate] (PHB), and succinic acid for poly(butylene succinate) (PBS). Moreover, several species of microorganisms that produce significant quantities of these functional chemicals under specific cultivation conditions from biomass-derived carbohydrates are also reviewed.Key words: functional chemicals, renewable resources, lactic acid, (R)-3-hydroxybutyric acid, succinic acid.
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Sauer M, Porro D, Mattanovich D, Branduardi P. Microbial production of organic acids: expanding the markets. Trends Biotechnol 2008; 26:100-8. [DOI: 10.1016/j.tibtech.2007.11.006] [Citation(s) in RCA: 460] [Impact Index Per Article: 28.8] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 09/30/2007] [Revised: 11/05/2007] [Accepted: 11/06/2007] [Indexed: 10/22/2022]
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Jantama K, Haupt M, Svoronos SA, Zhang X, Moore J, Shanmugam K, Ingram L. Combining metabolic engineering and metabolic evolution to develop nonrecombinant strains ofEscherichia coli C that produce succinate and malate. Biotechnol Bioeng 2008; 99:1140-53. [DOI: 10.1002/bit.21694] [Citation(s) in RCA: 262] [Impact Index Per Article: 16.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/10/2022]
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