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Umrigar V, Chakraborty M, Parikh PA. Optimization of microwave-assisted esterification of succinic acid using Box-Behnken design approach. ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH INTERNATIONAL 2023; 30:71472-71481. [PMID: 36088440 DOI: 10.1007/s11356-022-22807-1] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/30/2021] [Accepted: 08/26/2022] [Indexed: 06/14/2023]
Abstract
Esters of butanedioic acid (succinic acid) are appealing renewable esters as fuel additives and solvents. In the present study, we have investigated reaction routes for the esterification of succinic acid (SA) with alcohols like methanol (MeOH), ethanol (EtOH), and 2-propanol (2-PrOH) using heterogeneous catalyst D-Hβ (moderate Bronsted acidity) in a microwave (MW)-irradiated reactor to increase yield and minimize waste generation. Using the Box-Behnken design (BBD) approach, operating parameters such as reaction time, microwave power, and catalyst dosing were optimized for SA esterification with MeOH. At optimum conditions using D-Hβ catalyst, 99% maximum conversion was achieved with 98% selectivity of dimethyl succinate (DMS). At optimum conditions, the esterification of SA with EtOH and 2-PrOH was also performed. The use of D-Hβ is economically more advantageous as it can be reused directly without any prior washing and also showed significant activity.
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Affiliation(s)
- Vaishali Umrigar
- Chemical Engineering Department, Sarvajanik College of Engineering and Technology, Surat, 395001, India.
| | - Mousumi Chakraborty
- Department of Chemical Engineering, S.V. National Institute of Technology, Surat, 395007, India
| | - Parimal A Parikh
- Department of Chemical Engineering, S.V. National Institute of Technology, Surat, 395007, India
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Development of a Simple and Robust Kinetic Model for the Production of Succinic Acid from Glucose Depending on Different Operating Conditions. FERMENTATION-BASEL 2023. [DOI: 10.3390/fermentation9030222] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 03/02/2023]
Abstract
Succinic acid (SA) is one of the main identified biomass-derived chemical building blocks. In this work we approach the study of its production by Actinobacillus succinogenes DSM 22257 from glucose, focusing on the development and application of a simple kinetic model capable of representing the evolution of the process over time for a great diversity of process variables key to the production of this platform bio-based chemical: initial biomass concentration, yeast extract concentration, agitation speed, and carbon dioxide flow rate. All these variables were studied experimentally, determining the values of key fermentation parameters: titer (23.8–39.7 g·L−1), yield (0.59–0.72 gSA·gglu−1), productivity (0.48–0.96 gSA·L−1·h−1), and selectivity (0.61–0.69 gSA·gglu−1). Even with this wide diversity of operational conditions, a non-structured and non-segregated kinetic model was suitable for fitting to experimental data with high accuracy, considering the values of the goodness-of-fit statistical parameters. This model is based on the logistic equation for biomass growth and on potential kinetic equations to describe the evolution of SA and the sum of by-products as production events that are not associated with biomass growth. The application of the kinetic model to diverse operational conditions sheds light on their effect on SA production. It seems that nitrogen stress is a good condition for SA titer and selectivity, there is an optimal inoculum mass for this purpose, and hydrodynamic stress starts at 300 r.p.m. in the experimental set-up employed. Due to its practical importance, and to validate the developed kinetic model, a fed-batch fermentation was also carried out, verifying the goodness of the model proposed via the process simulation (stage or cycle 1) and application to further cycles of the fed-batch operation. The results showed that biomass inactivation started at cycle 3 after a grace period in cycle 2.
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Tsibranska I, Vlaev S, Dzhonova D, Tylkowski B, Panyovska S, Dermendzhieva N. Modeling and assessment of the transfer effectiveness in integrated bioreactor with membrane separation. PHYSICAL SCIENCES REVIEWS 2022. [DOI: 10.1515/psr-2020-0063] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [Abstract] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/15/2022]
Abstract
Abstract
Integrating a reaction process with membrane separation allows for effective product removal, favorable shifting of the reaction equilibrium, overcoming eventual inhibitory or toxic effects of the products and has the advantage of being energy and space saving. It has found a range of applications in innovative biotechnologies, generating value-added products (exopolysaccharides, antioxidants, carboxylic acids) with high potential for separation/ concentration of thermosensitive bioactive compounds, preserving their biological activity and reducing the amount of solvents and the energy for solvent recovery. Evaluating the effectiveness of such integrated systems is based on fluid dynamics and mass transfer knowledge of flowing matter close to the membrane surface – shear deformation rates and shear stress at the membrane interface, mass transfer coefficients. A Computational Fluid Dynamics (CFD)-based approach for assessing the effectiveness of integrated stirred tank bioreactor with submerged membrane module is compiled. It is related to the hydrodynamic optimization of the selected reactor configuration in two-phase flow, as well as to the concentration profiles and analysis of the reactor conditions in terms of reaction kinetics and mass transfer.
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Affiliation(s)
- Irene Tsibranska
- Institute of Chemical Engineering , Bulgarian Academy of Sciences , 1113 Sofia , Bulgaria
| | - Serafim Vlaev
- Institute of Chemical Engineering , Bulgarian Academy of Sciences , 1113 Sofia , Bulgaria
| | - Daniela Dzhonova
- Institute of Chemical Engineering , Bulgarian Academy of Sciences , 1113 Sofia , Bulgaria
| | - Bartosz Tylkowski
- Eurecat, Centre Tecnològic de Catalunya , C/Marcellí Domingo s/n , 43007 Tarragona , Spain
| | - Stela Panyovska
- Institute of Chemical Engineering , Bulgarian Academy of Sciences , 1113 Sofia , Bulgaria
| | - Nadezhda Dermendzhieva
- Institute of Chemical Engineering , Bulgarian Academy of Sciences , 1113 Sofia , Bulgaria
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Mancini E, Ramin P, Styrbæck P, Bjergholt C, Soheil Mansouri S, Gernaey KV, Luo J, Pinelo M. Separation of succinic acid from fermentation broth: Dielectric exclusion, Donnan effect and diffusion as the most influential mass transfer mechanisms. Sep Purif Technol 2022. [DOI: 10.1016/j.seppur.2021.119904] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/28/2022]
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Downstream separation and purification of bio-based alpha-ketoglutaric acid from post-fermentation broth using a multi-stage membrane process. Process Biochem 2020. [DOI: 10.1016/j.procbio.2020.05.026] [Citation(s) in RCA: 4] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Submit a Manuscript] [Subscribe] [Scholar Register] [Indexed: 02/04/2023]
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Antczak J, Szczygiełda M, Prochaska K. Nanofiltration separation of succinic acid from post-fermentation broth: Impact of process conditions and fouling analysis. J IND ENG CHEM 2019. [DOI: 10.1016/j.jiec.2019.04.046] [Citation(s) in RCA: 15] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/16/2022]
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MATSUMOTO M, TATSUMI M. Extraction and Esterification of Succinic Acid Using Aqueous Two-phase Systems Composed of Ethanol and Salts. SOLVENT EXTRACTION RESEARCH AND DEVELOPMENT-JAPAN 2018. [DOI: 10.15261/serdj.25.101] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.7] [Reference Citation Analysis] [Track Full Text] [Subscribe] [Scholar Register] [Indexed: 11/18/2022]
Affiliation(s)
- Michiaki MATSUMOTO
- Department of Chemical Engineering and Materials Science, Doshisha University
| | - Masahiro TATSUMI
- Department of Chemical Engineering and Materials Science, Doshisha University
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Law JY, Mohammad AW. Multiple-solute salts as draw solution for osmotic concentration of succinate feed by forward osmosis. J IND ENG CHEM 2017. [DOI: 10.1016/j.jiec.2017.03.011] [Citation(s) in RCA: 19] [Impact Index Per Article: 2.7] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
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Thuy NTH, Kongkaew A, Flood A, Boontawan A. Fermentation and crystallization of succinic acid from Actinobacillus succinogenes ATCC55618 using fresh cassava root as the main substrate. BIORESOURCE TECHNOLOGY 2017; 233:342-352. [PMID: 28285227 DOI: 10.1016/j.biortech.2017.02.114] [Citation(s) in RCA: 47] [Impact Index Per Article: 6.7] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/16/2016] [Revised: 02/23/2017] [Accepted: 02/24/2017] [Indexed: 05/25/2023]
Abstract
The fermentation of succinic acid from fresh cassava root using Actinobacillus succinogenes ATCC55618, and the recovery of the product using crystallization were investigated. Fresh cassava root is an ideal succinic acid feedstock due to its low price and high starch content. Saccharification was carried out using commercially available enzymes and diammonium phosphate was used as an inexpensive nitrogen source. Different fermentation modes were compared in terms of product yield and productivity. Results for fed-batch fermentations showed that a succinic acid titer of 151.44g/L, with yield and productivity of 1.51gSA/gglucose and 3.22g/L/h could be obtained. Seeded batch cooling crystallization was investigated after pre-treatment using nanofiltration. A succinic acid crystal purity of 99.35% with a relative crystallinity of 96.77% was obtained from high seeding experiments. These results indicated that fresh cassava roots could be an economically alternative feedstock for a high quality succinic acid production.
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Affiliation(s)
- Nguyen Thi Huong Thuy
- School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University avenue, Muang district, Nakhon Ratchasima 30000, Thailand
| | - Artit Kongkaew
- School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University avenue, Muang district, Nakhon Ratchasima 30000, Thailand
| | - Adrian Flood
- Department of Chemical and Biomolecular Engineering, Vidyasirimedhi Institute of Science and Technology (VISTEC), Wangchan District, Rayong 21210, Thailand
| | - Apichat Boontawan
- School of Biotechnology, Institute of Agricultural Technology, Suranaree University of Technology, 111 University avenue, Muang district, Nakhon Ratchasima 30000, Thailand; Cassava Research Center, Suranaree University of Technology, 111 University avenue, Muang district, Nakhon Ratchasima 30000, Thailand.
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Thuy NTH, Boontawan A. Production of very-high purity succinic acid from fermentation broth using microfiltration and nanofiltration-assisted crystallization. J Memb Sci 2017. [DOI: 10.1016/j.memsci.2016.11.073] [Citation(s) in RCA: 37] [Impact Index Per Article: 5.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/26/2022]
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Seth JR, Wangikar PP. Challenges and opportunities for microalgae-mediated CO2 capture and biorefinery. Biotechnol Bioeng 2015; 112:1281-96. [PMID: 25899427 DOI: 10.1002/bit.25619] [Citation(s) in RCA: 43] [Impact Index Per Article: 4.8] [Reference Citation Analysis] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 07/23/2014] [Revised: 03/31/2015] [Accepted: 04/07/2015] [Indexed: 11/10/2022]
Abstract
Aquacultures of microalgae are frontrunners for photosynthetic capture of CO2 from flue gases. Expedient implementation mandates coupling of microalgal CO2 capture with synthesis of fuels and organic products, so as to derive value from biomass. An integrated biorefinery complex houses a biomass growth and harvesting area and a refining zone for conversion to product(s) and separation to desired purity levels. As growth and downstream options require energy and incur loss of carbon, put together, the loop must be energy positive, carbon negative, or add substantial value. Feasibility studies can, thus, aid the choice from among the rapidly evolving technological options, many of which are still in the early phases of development. We summarize basic engineering calculations for the key steps of a biorefining loop where flue gases from a thermal power station are captured using microalgal biomass along with subsequent options for conversion to fuel or value added products. An assimilation of findings from recent laboratory and pilot-scale experiments and life cycle analysis (LCA) studies is presented as carbon and energy yields for growth and harvesting of microalgal biomass and downstream options. Of the biorefining options, conversion to the widely studied biofuel, ethanol, and manufacture of the platform chemical, succinic acid are presented. Both processes yield specific products and do not demand high-energy input but entail 60-70% carbon loss through fermentative respiration. Thermochemical conversions, on the other hand, have smaller carbon and energy losses but yield a mixture of products.
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Affiliation(s)
- Jyoti R Seth
- Department of Chemical Engineering, Indian Institute of Technology Bombay, Powai, Mumbai, India.,DBT-Pan IIT Center for Bioenergy, Indian Institute of Technology Bombay, Powai, Mumbai, India
| | - Pramod P Wangikar
- Department of Chemical Engineering, Indian Institute of Technology Bombay, Powai, Mumbai, India. .,DBT-Pan IIT Center for Bioenergy, Indian Institute of Technology Bombay, Powai, Mumbai, India. .,Wadhwani Research Center for Bioengineering, Indian Institute of Technology Bombay, Powai, Mumbai, 400076, India.
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