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Galindo-Rodriguez GR, Sarwar MS, Rios-Solis L, Dimartino S. Development, characterization and application of 3D printed adsorbents for in situ recovery of taxadiene from microbial cultivations. J Chromatogr A 2024; 1721:464815. [PMID: 38522406 DOI: 10.1016/j.chroma.2024.464815] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 01/25/2024] [Revised: 03/06/2024] [Accepted: 03/11/2024] [Indexed: 03/26/2024]
Abstract
Microbial cell factories are an attractive alternative to produce high-value natural products using sustainable processes. However, product recovery is one of the main challenges to reduce production cost and make these technologies economically interesting. In this work, new resins were formulated to 3D print hydrophobic adsorbents for the recovery of biologics from microbial cultivations. Benzyl methacrylate (BEMA) and butyl methacrylate (BUMA) were selected as functional monomers suitable for the adsorption of hydrophobic compounds. Pore morphology was tailored through the inclusion of pore forming agents (porogens) in the resin. Different porogens and porogen concentrations were evaluated resulting in materials with different porous networks. Sudan 1 and the anticancer drug paclitaxel were employed as model compounds to test the adsorption performance of hydrophobic and terpene molecules onto the developed 3D printed materials. The material with greatest adsorption capacity was obtained using BEMA monomer with 40 % (v/v) porogen (BEMA40). The performance of BEMA40 to recover taxadiene from small-scale (5 mL) Saccharomyces cerevisiae cultivations was tested and compared with commercial Diaion HP-20 beads. Taxadiene titres on BEMA40 (46 ± 2 mg/L) and Diaion HP-20 (54 ± 4 mg/L) were comparable, with no taxadiene detected in the cells and cell-free media, suggesting near 100 % taxadiene partition on the adsorbents. Compared to commercial beads, 3D printed adsorbents can be customized with adjustments in the resin formulation, are well adaptable to diverse bioreactor types, do not clog sampling ports and columns and are easier to handle during post processing. The results of this work demonstrate the potential of 3D printing to fabricate hydrophobic interaction adsorbent materials and their application in the recovery of biological products.
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Affiliation(s)
| | - M Sulaiman Sarwar
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh EH9 3BF, United Kingdom
| | - Leonardo Rios-Solis
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh EH9 3BF, United Kingdom; Centre for Engineering Biology, The University of Edinburgh, Edinburgh EH9 3BF, United Kingdom
| | - Simone Dimartino
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh EH9 3BF, United Kingdom.
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Galindo-Rodriguez GR, Santoyo-Garcia JH, Rios-Solis L, Dimartino S. In situ recovery of taxadiene using solid adsorption in cultivations with Saccharomyces cerevisiae. Prep Biochem Biotechnol 2024; 54:86-94. [PMID: 37162336 DOI: 10.1080/10826068.2023.2207204] [Citation(s) in RCA: 0] [Impact Index Per Article: 0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 05/11/2023]
Abstract
In this study, an engineered strain of Saccharomyces cerevisiae was used to produce taxadiene, a precursor in the biosynthetic pathway of the anticancer drug paclitaxel. Taxadiene was recovered in situ with the polymeric adsorbent Diaion © HP-20. Here we tested two bioreactor configurations and adsorbent concentrations to maximize the production and recovery of taxadiene. An external recovery configuration (ERC) was performed with the integration of an expanded bed adsorption column, whereas the internal recovery configuration (IRC) consisted in dispersed beads inside the bioreactor vessel. Taxadiene titers recovered in IRC were higher to ERC by 3.4 and 3.5 fold by using 3% and 12% (w/v) adsorbent concentration respectively. On the other hand, cell growth kinetics were faster in ERC which represents an advantage in productivity (mg of taxadiene/L*h). High resin bead concentration (12% w/v) improved the partition of taxadiene onto the beads up to 98%. This result represents an advantage over previous studies using a 3% resin concentration where the partition of taxadiene on the beads was around 50%. This work highlights the potential of in situ product recovery to improve product partition, reduce processing steps and promote cell growth. Nevertheless, a careful design of bioreactor configuration and process conditions is critical.
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Affiliation(s)
| | - Jorge H Santoyo-Garcia
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh, UK
- Centre for Synthetic and Systems Biology (SynthSys), The University of Edinburgh, Edinburgh, UK
| | - Leonardo Rios-Solis
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh, UK
- Centre for Synthetic and Systems Biology (SynthSys), The University of Edinburgh, Edinburgh, UK
| | - Simone Dimartino
- Institute for Bioengineering, School of Engineering, The University of Edinburgh, Edinburgh, UK
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Santoyo-Garcia JH, Valdivia-Cabrera M, Ochoa-Villarreal M, Casasola-Zamora S, Ripoll M, Escrich A, Moyano E, Betancor L, Halliday KJ, Loake GJ, Rios-Solis L. Increased paclitaxel recovery from Taxus baccata vascular stem cells using novel in situ product recovery approaches. BIORESOUR BIOPROCESS 2023; 10:68. [PMID: 38647629 PMCID: PMC10991628 DOI: 10.1186/s40643-023-00687-8] [Citation(s) in RCA: 1] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Grants] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 04/29/2023] [Accepted: 09/16/2023] [Indexed: 04/25/2024] Open
Abstract
In this study, several approaches were tested to optimise the production and recovery of the widely used anticancer drug Taxol® (paclitaxel) from culturable vascular stem cells (VSCs) of Taxus baccata, which is currently used as a successful cell line for paclitaxel production. An in situ product recovery (ISPR) technique was employed, which involved combining three commercial macro-porous resin beads (HP-20, XAD7HP and HP-2MG) with batch and semi-continuous cultivations of the T. baccata VSCs after adding methyl jasmonate (Me-JA) as an elicitor. The optimal resin combination resulted in 234 ± 23 mg of paclitaxel per kg of fresh-weight cells, indicating a 13-fold improved yield compared to the control (with no resins) in batch cultivation. This resin treatment was further studied to evaluate the resins' removal capacity of reactive oxygen species (ROS), which can cause poor cell growth or reduce product synthesis. It was observed that the ISPR cultivations had fourfold less intracellular ROS concentration than that of the control; thus, a reduced ROS concentration established by the resin contributed to increased paclitaxel yield, contrary to previous studies. These paclitaxel yields are the highest reported to date using VSCs, and this scalable production method could be applied for a diverse range of similar compounds utilising plant cell culture.
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Affiliation(s)
- Jorge H Santoyo-Garcia
- Institute for Bioengineering, School of Engineering, University of Edinburgh, King's Buildings, Edinburgh, EH9 3FB, UK.
- Centre for Engineering Biology, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK.
| | - Marissa Valdivia-Cabrera
- Institute of Molecular Plant Sciences, School of Biological Sciences, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK
| | - Marisol Ochoa-Villarreal
- Institute of Molecular Plant Sciences, School of Biological Sciences, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK
| | | | - Magdalena Ripoll
- Laboratorio de Biotecnología, Universidad ORT Uruguay, Mercedes 1237, 11100, Montevideo, Uruguay
- Graduate Program in Chemistry, Facultad de Química, Universidad de la República, Montevideo, Uruguay
| | - Ainoa Escrich
- Department of Medicine and Life Sciences, Universitat Pompeu Fabra, 08003, Barcelona, Spain
| | - Elisabeth Moyano
- Department of Medicine and Life Sciences, Universitat Pompeu Fabra, 08003, Barcelona, Spain
| | - Lorena Betancor
- Laboratorio de Biotecnología, Universidad ORT Uruguay, Mercedes 1237, 11100, Montevideo, Uruguay
| | - Karen J Halliday
- Institute of Molecular Plant Sciences, School of Biological Sciences, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK
| | - Gary J Loake
- Institute of Molecular Plant Sciences, School of Biological Sciences, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK
- Green Bioactives, Douglas House, Pentland Science Park, Midlothian, EH16 0PL, UK
| | - Leonardo Rios-Solis
- Institute for Bioengineering, School of Engineering, University of Edinburgh, King's Buildings, Edinburgh, EH9 3FB, UK.
- Centre for Engineering Biology, University of Edinburgh, King's Buildings, Edinburgh, EH9 3BF, UK.
- School of Natural and Environmental Sciences, Molecular Biology and Biotechnology Division, Newcastle University, Newcastle upon Tyne, NE1 7RU, UK.
- Department of Biochemical Engineering, The Advanced Centre for Biochemical Engineering, University College London, Gower Street, London, WC1E 6BT, UK.
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Vamsi Krishna K, Bharathi N, George Shiju S, Alagesan Paari K, Malaviya A. An updated review on advancement in fermentative production strategies for biobutanol using Clostridium spp. Environ Sci Pollut Res Int 2022; 29:47988-48019. [PMID: 35562606 DOI: 10.1007/s11356-022-20637-9] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 12/12/2021] [Accepted: 04/30/2022] [Indexed: 06/15/2023]
Abstract
A significant concern of our fuel-dependent era is the unceasing exhaustion of petroleum fuel supplies. In parallel to this, environmental issues such as the greenhouse effect, change in global climate, and increasing global temperature must be addressed on a priority basis. Biobutanol, which has fuel characteristics comparable to gasoline, has attracted global attention as a viable green fuel alternative among the many biofuel alternatives. Renewable biomass could be used for the sustainable production of biobutanol by the acetone-butanol-ethanol (ABE) pathway. Non-extinguishable resources, such as algal and lignocellulosic biomass, and starch are some of the most commonly used feedstock for fermentative production of biobutanol, and each has its particular set of advantages. Clostridium, a gram-positive endospore-forming bacterium that can produce a range of compounds, along with n-butanol is traditionally known for its biobutanol production capabilities. Clostridium fermentation produces biobased n-butanol through ABE fermentation. However, low butanol titer, a lack of suitable feedstock, and product inhibition are the primary difficulties in biobutanol synthesis. Critical issues that are essential for sustainable production of biobutanol include (i) developing high butanol titer producing strains utilizing genetic and metabolic engineering approaches, (ii) renewable biomass that could be used for biobutanol production at a larger scale, and (iii) addressing the limits of traditional batch fermentation by integrated bioprocessing technologies with effective product recovery procedures that have increased the efficiency of biobutanol synthesis. Our paper reviews the current progress in all three aspects of butanol production and presents recent data on current practices in fermentative biobutanol production technology.
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Affiliation(s)
- Kondapalli Vamsi Krishna
- Applied and Industrial Biotechnology Laboratory, CHRIST (Deemed-to-Be University), Hosur road, Bangalore, Karnataka, India
| | - Natarajan Bharathi
- Department of Life Sciences, CHRIST (Deemed to Be University), Bengaluru, India
| | - Shon George Shiju
- Applied and Industrial Biotechnology Laboratory, CHRIST (Deemed-to-Be University), Hosur road, Bangalore, Karnataka, India
| | | | - Alok Malaviya
- Applied and Industrial Biotechnology Laboratory, CHRIST (Deemed-to-Be University), Hosur road, Bangalore, Karnataka, India.
- Department of Life Sciences, CHRIST (Deemed to Be University), Bengaluru, India.
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Mindt M, Beyraghdar Kashkooli A, Suarez-Diez M, Ferrer L, Jilg T, Bosch D, Martins Dos Santos V, Wendisch VF, Cankar K. Production of indole by Corynebacterium glutamicum microbial cell factories for flavor and fragrance applications. Microb Cell Fact 2022; 21:45. [PMID: 35331232 PMCID: PMC8944080 DOI: 10.1186/s12934-022-01771-y] [Citation(s) in RCA: 3] [Impact Index Per Article: 1.5] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 02/01/2022] [Accepted: 03/01/2022] [Indexed: 02/07/2023] Open
Abstract
Background The nitrogen containing aromatic compound indole is known for its floral odor typical of jasmine blossoms. Due to its characteristic scent, it is frequently used in dairy products, tea drinks and fine fragrances. The demand for natural indole by the flavor and fragrance industry is high, yet, its abundance in essential oils isolated from plants such as jasmine and narcissus is low. Thus, there is a strong demand for a sustainable method to produce food-grade indole. Results Here, we established the biotechnological production of indole upon l-tryptophan supplementation in the bacterial host Corynebacterium glutamicum. Heterologous expression of the tryptophanase gene from E. coli enabled the conversion of supplemented l-tryptophan to indole. Engineering of the substrate import by co-expression of the native aromatic amino acid permease gene aroP increased whole-cell biotransformation of l-tryptophan to indole by two-fold. Indole production to 0.2 g L−1 was achieved upon feeding of 1 g L−1l-tryptophan in a bioreactor cultivation, while neither accumulation of side-products nor loss of indole were observed. To establish an efficient and robust production process, new tryptophanases were recruited by mining of bacterial sequence databases. This search retrieved more than 400 candidates and, upon screening of tryptophanase activity, nine new enzymes were identified as most promising. The highest production of indole in vivo in C. glutamicum was achieved based on the tryptophanase from Providencia rettgeri. Evaluation of several biological aspects identified the product toxicity as major bottleneck of this conversion. In situ product recovery was applied to sequester indole in a food-grade organic phase during the fermentation to avoid inhibition due to product accumulation. This process enabled complete conversion of l-tryptophan and an indole product titer of 5.7 g L−1 was reached. Indole partitioned to the organic phase which contained 28 g L−1 indole while no other products were observed indicating high indole purity. Conclusions The bioconversion production process established in this study provides an attractive route for sustainable indole production from tryptophan in C. glutamicum. Industrially relevant indole titers were achieved within 24 h and indole was concentrated in the organic layer as a pure product after the fermentation. Supplementary Information The online version contains supplementary material available at 10.1186/s12934-022-01771-y.
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Affiliation(s)
- Melanie Mindt
- Business Unit Bioscience, Wageningen Plant Research, Wageningen University & Research, Wageningen, The Netherlands.,Axxence Aromatic GmbH, Emmerich am Rhein, Germany
| | - Arman Beyraghdar Kashkooli
- Business Unit Bioscience, Wageningen Plant Research, Wageningen University & Research, Wageningen, The Netherlands
| | - Maria Suarez-Diez
- Laboratory of Systems and Synthetic Biology, Wageningen University & Research, Wageningen, The Netherlands
| | - Lenny Ferrer
- Genetics of Prokaryotes, Faculty of Biology & CeBiTec, Bielefeld University, Bielefeld, Germany
| | - Tatjana Jilg
- Genetics of Prokaryotes, Faculty of Biology & CeBiTec, Bielefeld University, Bielefeld, Germany
| | - Dirk Bosch
- Business Unit Bioscience, Wageningen Plant Research, Wageningen University & Research, Wageningen, The Netherlands
| | - Vitor Martins Dos Santos
- Laboratory of Systems and Synthetic Biology, Wageningen University & Research, Wageningen, The Netherlands.,Laboratory of Bioprocess Engineering, Wageningen University & Research, Wageningen, The Netherlands
| | - Volker F Wendisch
- Genetics of Prokaryotes, Faculty of Biology & CeBiTec, Bielefeld University, Bielefeld, Germany
| | - Katarina Cankar
- Business Unit Bioscience, Wageningen Plant Research, Wageningen University & Research, Wageningen, The Netherlands.
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Combes J, Imatoukene N, Couvreur J, Godon B, Brunissen F, Fojcik C, Allais F, Lopez M. Intensification of p-coumaric acid heterologous production using extractive biphasic fermentation. Bioresour Technol 2021; 337:125436. [PMID: 34182346 DOI: 10.1016/j.biortech.2021.125436] [Citation(s) in RCA: 11] [Impact Index Per Article: 3.7] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 05/08/2021] [Revised: 06/14/2021] [Accepted: 06/16/2021] [Indexed: 06/13/2023]
Abstract
p-coumaric acid (p-CA) can be produced from D-glucose by an engineered S. cerevisiae strain. p-CA has antimicrobial properties and retro-inhibition activity. Moreover, p-CA is a hydrophobic compound, limiting its accumulation in fermentation broth. To overcome these issues all at once, a liquid-liquid extraction in-situ product recovery process using oleyl alcohol as extractant has been implemented in order to continuously extract p-CA from the broth. Media and pH impacts on strain metabolism were assessed, highlighting p-CA decarboxylase endogenous activity. Biphasic fermentations allowed an increase in p-CA respiratory production rates at both pH assessed (13.65 and 9.45 mg L-1.h-1 at pH 6 and 4.5, respectively) compared to control ones (10.5 and 7.5 mg L-1.h-1 at pH 6 and 4.5, respectively). Biphasic fermentation effects on p-CA decarboxylation were studied showing that continuous removal of p-CA decreased its decarboxylation into 4-vinylphenol at pH 4.5 (57 mg L-1 in biphasic fermentation vs 173 mg L-1 in control one).
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Affiliation(s)
- Jeanne Combes
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | - Nabila Imatoukene
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | - Julien Couvreur
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | - Blandine Godon
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | - Fanny Brunissen
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | | | - Florent Allais
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France
| | - Michel Lopez
- URD Agro-Biotechnologies Industrielles (ABI), CEBB, AgroParisTech, Pomacle 51110, France.
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Outram V, Zhang Y. Solvent-free membrane extraction of volatile fatty acids from acidogenic fermentation. Bioresour Technol 2018; 270:400-408. [PMID: 30245308 DOI: 10.1016/j.biortech.2018.09.057] [Citation(s) in RCA: 6] [Impact Index Per Article: 1.0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 08/06/2018] [Revised: 09/10/2018] [Accepted: 09/11/2018] [Indexed: 06/08/2023]
Abstract
Diversification of anaerobic digestion into higher value products, namely volatile fatty acids (VFAs), is receiving interest. One of the biggest challenges with this is recovery of the VFAs. Membrane extraction can be used, and a novel process configuration using a non-porous silicone membrane and water for an extractant is proposed here. This process would enable the reduction in the number of downstream unit operations compared to other membrane extraction processes. Selective recovery in favour of longer chain VFAs was demonstrated. Testing with a synthetic solution resulted in an overall mass transfer coefficient of 0.088 μm s-1 for butyric acid, and 0.157 μm s-1 when fermentation broth was used. This indicates this process is not hindered by fouling, but improved somehow. Although the preliminary economic analysis showed this process to require a larger membrane area compared to porous membrane alternatives, it also has a significantly reduced cost associated with the extractant.
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Affiliation(s)
- Victoria Outram
- Faculty of Engineering and Physical Sciences, University of Southampton, Southampton, UK.
| | - Yue Zhang
- Faculty of Engineering and Physical Sciences, University of Southampton, Southampton, UK
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8
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Wen H, Chen H, Cai D, Gong P, Zhang T, Wu Z, Gao H, Li Z, Qin P, Tan T. Integrated in situ gas stripping-salting-out process for high-titer acetone-butanol-ethanol production from sweet sorghum bagasse. Biotechnol Biofuels 2018; 11:134. [PMID: 29760776 PMCID: PMC5944105 DOI: 10.1186/s13068-018-1137-5] [Citation(s) in RCA: 7] [Impact Index Per Article: 1.2] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Figures] [Subscribe] [Scholar Register] [Received: 07/14/2017] [Accepted: 05/02/2018] [Indexed: 06/08/2023]
Abstract
BACKGROUND The production of biobutanol from renewable biomass resources is attractive. The energy-intensive separation process and low-titer solvents production are the key constraints on the economy-feasible acetone-butanol-ethanol (ABE) production by fermentation. To decrease energy consumption and increase the solvents concentration, a novel two-stage gas stripping-salting-out system was established for effective ABE separation from the fermentation broth using sweet sorghum bagasse as feedstock. RESULTS The ABE condensate (143.6 g/L) after gas stripping, the first-stage separation, was recovered and introduced to salting-out process as the second-stage. K4P2O7 and K2HPO4 were used, respectively. The effect of saturated salt solution temperature on final ABE concentration was also investigated. The results showed high ABE recovery (99.32%) and ABE concentration (747.58 g/L) when adding saturated K4P2O7 solution at 323.15 K and 3.0 of salting-out factor. On this condition, the energy requirement of the downstream distillation process was 3.72 MJ/kg of ABE. CONCLUSIONS High-titer cellulosic ABE production was separated from the fermentation broth by the novel two-stage gas stripping-salting-out process. The process was effective, which reduced the downstream process energy requirement significantly.
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Affiliation(s)
- Hao Wen
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, No. 15 Beisanhuan East Road, Chaoyang District, Beijing, 100029 People’s Republic of China
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Huidong Chen
- College of Chemical Engineering, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
- Center for Process Simulation & Optimization, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Di Cai
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, No. 15 Beisanhuan East Road, Chaoyang District, Beijing, 100029 People’s Republic of China
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Peiwen Gong
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Tao Zhang
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Zhichao Wu
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Heting Gao
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Zhuangzhuang Li
- College of Chemical Engineering, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Peiyong Qin
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, No. 15 Beisanhuan East Road, Chaoyang District, Beijing, 100029 People’s Republic of China
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
| | - Tianwei Tan
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, No. 15 Beisanhuan East Road, Chaoyang District, Beijing, 100029 People’s Republic of China
- College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029 People’s Republic of China
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9
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Zhu C, Chen L, Xue C, Bai F. A novel close-circulating vapor stripping-vapor permeation technique for boosting biobutanol production and recovery. Biotechnol Biofuels 2018; 11:128. [PMID: 29755587 PMCID: PMC5934881 DOI: 10.1186/s13068-018-1129-5] [Citation(s) in RCA: 18] [Impact Index Per Article: 3.0] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Grants] [Track Full Text] [Subscribe] [Scholar Register] [Received: 02/03/2018] [Accepted: 04/23/2018] [Indexed: 05/31/2023]
Abstract
BACKGROUND Butanol derived from renewable resources by microbial fermentation is considered as one of not only valuable platform chemicals but alternative advanced biofuels. However, due to low butanol concentration in fermentation broth, butanol production is restricted by high energy consumption for product recovery. For in situ butanol recovery techniques, such as gas stripping and pervaporation, the common problem is their low efficiency in harvesting and concentrating butanol. Therefore, there is a necessity to develop an advanced butanol recovery technique for cost-effective biobutanol production. RESULTS A close-circulating vapor stripping-vapor permeation (VSVP) process was developed with temperature-difference control for single-stage butanol recovery. In the best scenario, the highest butanol separation factor of 142.7 reported to date could be achieved with commonly used polydimethylsiloxane membrane, when temperatures of feed solution and membrane surroundings were 70 and 0 °C, respectively. Additionally, more ABE (31.2 vs. 17.7 g/L) were produced in the integrated VSVP process, with a higher butanol yield (0.21 vs. 0.17 g/g) due to the mitigation of butanol inhibition. The integrated VSVP process generated a highly concentrated permeate containing 212.7 g/L butanol (339.3 g/L ABE), with the reduced energy consumption of 19.6 kJ/g-butanol. CONCLUSIONS Therefore, the present study demonstrated a well-designed energy-efficient technique named by vapor stripping-vapor permeation for single-stage butanol removal. The butanol separation factor was multiplied by the temperature-difference control strategy which could double butanol recovery performance. This advanced VSVP process can completely eliminate membrane fouling risk for fermentative butanol separation, which is superior to other techniques.
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Affiliation(s)
- Chao Zhu
- School of Life Science and Biotechnology, Dalian University of Technology, No 2 Linggong Road, Dalian, 116024 China
| | - Lijie Chen
- School of Life Science and Biotechnology, Dalian University of Technology, No 2 Linggong Road, Dalian, 116024 China
| | - Chuang Xue
- School of Life Science and Biotechnology, Dalian University of Technology, No 2 Linggong Road, Dalian, 116024 China
| | - Fengwu Bai
- School of Life Science and Biotechnology, Dalian University of Technology, No 2 Linggong Road, Dalian, 116024 China
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10
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Alemdar S, König JC, Hartwig S, Frister T, Scheper T, Beutel S. Bioproduction of α-humulene in metabolically engineered Escherichia coli and application in zerumbone synthesis. Eng Life Sci 2017; 17:900-907. [PMID: 32624838 DOI: 10.1002/elsc.201700043] [Citation(s) in RCA: 12] [Impact Index Per Article: 1.7] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 02/28/2017] [Revised: 06/02/2017] [Accepted: 06/06/2017] [Indexed: 01/09/2023] Open
Abstract
Zerumbone is a sesquiterpene ketone with potent anti-cancerogenic activities, produced in several ginger species of the Zingiberaceae familiy. We have investigated the biotechnological production of α-humulene, a precursor of zerumbone. By implementing a heterologous mevalonate pathway in combination with the α-humulene synthase expression, we effectively synthesized α-humulene from glucose in Escherichia coli. In this study, we developed a practical and efficient in situ separation method for α-humulene by comparison of extractive and adsorptive strategies. By the in situ adsorption of the product to the hydrophobic resin Amberlite® XAD4 we were able to increase α-humulene yield by 2310% to 60.2 mg/L. Furthermore we present an easy applicable, short subsequent chemical process for the conversion of α-humulene to zerumbone by using transition metal catalysis. To reduce process steps, the chemical reaction was carried out in the same solvent as the eluting solvent that was used to elute α-humulene from the adsorbent resin. By allylic oxidation of α-humulene with manganeseII chloride as a catalyst and tert.-butylhydroperoxide as an oxidizing agent we were able to synthetize zerumbone with a selectivity of 51.6%. Product and byproducts of the oxidation reaction were identified by GC-MS.
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Affiliation(s)
- Semra Alemdar
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
| | - Jan C König
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
| | - Steffen Hartwig
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
| | - Thore Frister
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
| | - Thomas Scheper
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
| | - Sascha Beutel
- Leibniz University Hannover Institute of Technical Chemistry Hannover Germany
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11
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Outram V, Lalander CA, Lee JGM, Davies ET, Harvey AP. Applied in situ product recovery in ABE fermentation. Biotechnol Prog 2017; 33:563-579. [PMID: 28188696 PMCID: PMC5485034 DOI: 10.1002/btpr.2446] [Citation(s) in RCA: 52] [Impact Index Per Article: 7.4] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/14/2016] [Revised: 01/31/2017] [Indexed: 12/12/2022]
Abstract
The production of biobutanol is hindered by the product's toxicity to the bacteria, which limits the productivity of the process. In situ product recovery of butanol can improve the productivity by removing the source of inhibition. This paper reviews in situ product recovery techniques applied to the acetone butanol ethanol fermentation in a stirred tank reactor. Methods of in situ recovery include gas stripping, vacuum fermentation, pervaporation, liquid–liquid extraction, perstraction, and adsorption, all of which have been investigated for the acetone, butanol, and ethanol fermentation. All techniques have shown an improvement in substrate utilization, yield, productivity or both. Different fermentation modes favored different techniques. For batch processing gas stripping and pervaporation were most favorable, but in fed‐batch fermentations gas stripping and adsorption were most promising. During continuous processing perstraction appeared to offer the best improvement. The use of hybrid techniques can increase the final product concentration beyond that of single‐stage techniques. Therefore, the selection of an in situ product recovery technique would require comparable information on the energy demand and economics of the process. © 2017 American Institute of Chemical Engineers Biotechnol. Prog., 33:563–579, 2017
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Affiliation(s)
- Victoria Outram
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne, U.K.,Green Biologics Ltd, 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, U.K
| | - Carl-Axel Lalander
- Green Biologics Ltd, 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, U.K
| | - Jonathan G M Lee
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne, U.K
| | - E Timothy Davies
- Green Biologics Ltd, 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, U.K
| | - Adam P Harvey
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne, U.K
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Cai D, Hu S, Miao Q, Chen C, Chen H, Zhang C, Li P, Qin P, Tan T. Two-stage pervaporation process for effective in situ removal acetone-butanol-ethanol from fermentation broth. Bioresour Technol 2017; 224:380-388. [PMID: 27839857 DOI: 10.1016/j.biortech.2016.11.010] [Citation(s) in RCA: 30] [Impact Index Per Article: 4.3] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 08/31/2016] [Revised: 11/02/2016] [Accepted: 11/03/2016] [Indexed: 06/06/2023]
Abstract
Two-stage pervaporation for ABE recovery from fermentation broth was studied to reduce the energy cost. The permeate after the first stage in situ pervaporation system was further used as the feedstock in the second stage of pervaporation unit using the same PDMS/PVDF membrane. A total 782.5g/L of ABE (304.56g/L of acetone, 451.98g/L of butanol and 25.97g/L of ethanol) was achieved in the second stage permeate, while the overall acetone, butanol and ethanol separation factors were: 70.7-89.73, 70.48-84.74 and 9.05-13.58, respectively. Furthermore, the theoretical evaporation energy requirement for ABE separation in the consolidate fermentation, which containing two-stage pervaporation and the following distillation process, was estimated less than ∼13.2MJ/kg-butanol. The required evaporation energy was only 36.7% of the energy content of butanol. The novel two-stage pervaporation process was effective in increasing ABE production and reducing energy consumption of the solvents separation system.
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Affiliation(s)
- Di Cai
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Song Hu
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Qi Miao
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Changjing Chen
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Huidong Chen
- College of Chemical Engineering, Beijing University of Chemical Technology, Beijing 100029, PR China; Center for Process Simulation & Optimization, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Changwei Zhang
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Ping Li
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
| | - Peiyong Qin
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China.
| | - Tianwei Tan
- National Energy R&D Center for Biorefinery, Beijing University of Chemical Technology, Beijing 100029, PR China
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Xue C, Liu F, Xu M, Tang IC, Zhao J, Bai F, Yang ST. Butanol production in acetone-butanol-ethanol fermentation with in situ product recovery by adsorption. Bioresour Technol 2016; 219:158-168. [PMID: 27484672 DOI: 10.1016/j.biortech.2016.07.111] [Citation(s) in RCA: 55] [Impact Index Per Article: 6.9] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/13/2016] [Revised: 07/25/2016] [Accepted: 07/26/2016] [Indexed: 06/06/2023]
Abstract
Activated carbon Norit ROW 0.8, zeolite CBV901, and polymeric resins Dowex Optipore L-493 and SD-2 with high specific loadings and partition coefficients were studied for n-butanol adsorption. Adsorption isotherms were found to follow Langmuir model, which can be used to estimate the amount of butanol adsorbed in acetone-butanol-ethanol (ABE) fermentation. In serum-bottle fermentation with in situ adsorption, activated carbon showed the best performance with 21.9g/L of butanol production. When operated in a fermentor, free- and immobilized-cell fermentations with adsorption produced 31.6g/L and 54.6g/L butanol with productivities of 0.30g/L·h and 0.45g/L·h, respectively. Thermal desorption produced a condensate containing ∼167g/L butanol, which resulted in a highly concentrated butanol solution of ∼640g/L after spontaneous phase separation. This in situ product recovery process with activated carbon is energy efficient and can be easily integrated with ABE fermentation for n-butanol production.
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Affiliation(s)
- Chuang Xue
- Department of Life Science and Biotechnology, Dalian University of Technology, Dalian 116024, China; Department of Chemical and Biomolecular Engineering, The Ohio State University, 151 West Woodruff Avenue, Columbus, OH 43210, USA
| | - Fangfang Liu
- Department of Chemical and Biomolecular Engineering, The Ohio State University, 151 West Woodruff Avenue, Columbus, OH 43210, USA
| | - Mengmeng Xu
- Department of Chemical and Biomolecular Engineering, The Ohio State University, 151 West Woodruff Avenue, Columbus, OH 43210, USA
| | - I-Ching Tang
- Bioprocessing Innovative Company, 4734 Bridle Path Court, Dublin, OH 43017, USA
| | - Jingbo Zhao
- Department of Chemical and Biomolecular Engineering, The Ohio State University, 151 West Woodruff Avenue, Columbus, OH 43210, USA
| | - Fengwu Bai
- Department of Life Science and Biotechnology, Dalian University of Technology, Dalian 116024, China
| | - Shang-Tian Yang
- Department of Chemical and Biomolecular Engineering, The Ohio State University, 151 West Woodruff Avenue, Columbus, OH 43210, USA.
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Outram V, Lalander CA, Lee JGM, Davis ET, Harvey AP. A comparison of the energy use of in situ product recovery techniques for the Acetone Butanol Ethanol fermentation. Bioresour Technol 2016; 220:590-600. [PMID: 27619710 DOI: 10.1016/j.biortech.2016.09.002] [Citation(s) in RCA: 15] [Impact Index Per Article: 1.9] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 06/29/2016] [Revised: 08/31/2016] [Accepted: 09/01/2016] [Indexed: 06/06/2023]
Abstract
The productivity of the Acetone Butanol Ethanol (ABE) fermentation can be significantly increased by application of various in situ product recovery (ISPR) techniques. There are numerous technically viable processes, but it is not clear which is the most economically viable in practice. There is little available information about the energy requirements and economics of ISPR for the ABE fermentation. This work compares various ISPR techniques based on UniSim process simulations of the ABE fermentation. The simulations provide information on the process energy and separation efficiency, which is fed into an economic assessment. Perstraction was the only technique to reduce the energy demand below that of a batch process, by approximately 5%. Perstraction also had the highest profit increase over a batch process, by 175%. However, perstraction is an immature technology, so would need significant development before being integrated to an industrial process.
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Affiliation(s)
- Victoria Outram
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne NE1 7RU, UK; Green Biologics Ltd., 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, UK.
| | - Carl-Axel Lalander
- Green Biologics Ltd., 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, UK
| | - Jonathan G M Lee
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne NE1 7RU, UK
| | - E Timothy Davis
- Green Biologics Ltd., 45A Western Avenue, Milton Park, Abingdon, Oxfordshire, UK
| | - Adam P Harvey
- School of Chemical Engineering and Advanced Material, Newcastle University, Newcastle-upon-Tyne NE1 7RU, UK
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Meier K, Djeljadini S, Regestein L, Büchs J, Carstensen F, Wessling M, Holland T, Raven N. In situ cell retention of a CHO culture by a reverse-flow diafiltration membrane bioreactor. Biotechnol Prog 2014; 30:1348-55. [PMID: 25202924 DOI: 10.1002/btpr.1988] [Citation(s) in RCA: 3] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [What about the content of this article? (0)] [Affiliation(s)] [Abstract] [Key Words] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 06/24/2014] [Revised: 08/28/2014] [Indexed: 11/10/2022]
Abstract
Heterogeneities occur in various bioreactor designs including cell retention devices. Whereas in external devices changing environmental conditions cannot be prevented, cells are retained in their optimal environment in internal devices. Conventional reverse-flow diafiltration utilizes an internal membrane device, but pulsed feeding causes temporal heterogeneities. In this study, the influence of conventional reverse-flow diafiltration on the yeast Hansenula polymorpha is investigated. Alternating 180 s of feeding with 360 s of non-feeding at a dilution rate of 0.2 h(-1) results in an oscillating DOT signal with an amplitude of 60%. Thereby, induced short-term oxygen limitations result in the formation of ethanol and a reduced product concentration of 25%. This effect is enforced at increased dilution rate. To overcome this cyclic problem, sequential operation of three membranes is introduced. Thus, quasi-continuous feeding is achieved reducing the oscillation of the DOT signal to an amplitude of 20% and 40% for a dilution rate of 0.2 h(-1) and 0.5 h(-1) , respectively. Fermentation conditions characterized by complete absence of oxygen limitation and without formation of overflow metabolites could be obtained for dilution rates from 0.1 h(-1) - 0.5 h(-1) . Thus, sequential operation of three membranes minimizes oscillations in the DOT signal providing a nearly homogenous culture over time.
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Affiliation(s)
- Kristina Meier
- RWTH Aachen, AVT-Biochemical Engineering, Worringer Weg 1, Aachen, 52074, Germany
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