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Integrated production for biodiesel and 1,3-propanediol with lipase-catalyzed transesterification and fermentation 总被引:2,自引:0,他引:2
Yunzhen Xu Hongjuan Liu Wei Du Yan Sun Xianjin Ou Dehua Liu 《Biotechnology letters》2009,31(9):1335-1341
Biodiesel, a renewable alternative to fossil energy, has shown great prospects for global proliferation in the past decade.
Lipase catalyzed transesterification for biodiesel production, as a biological process with many advantages has drawn increasing
attention. As a by-product, glycerol accounts for about 10% w/w of biodiesel during the process of biodiesel production. As
a result, the conversion of glycerol has become a common problem which has to be resolved if considering large amount of biodiesel
production. Glycerol can be fermented into 1,3-propanediol, a high value added chemical with a promising future in the polymers,
for example, polytrimethylene terephthalate, and also fermentation approaches for 1,3-propanediol production which have drawn
more and more attention due to advantages such as relatively low investment, mild reaction conditions and using renewable
sources as the starting materials. Based on the latest technology advancements in lipase-mediated transformation for biodiesel
production, the aerobic fermentation technology and genetic engineering for 1,3-propanediol production, and the integrated
production of 1,3-propanediol from crude glycerol could be a promising way to improve the profit of the whole process during
biodiesel production. 相似文献
3.
Biopolymers can be a green alternative to fossil-based polymers and can contribute to environmental protection because they are produced using renewable raw materials. Biopolymers are composed of various small subunits (building blocks) that are the intermediates or end products of major metabolic pathways. Most building blocks are secreted directly outside of cells, making downstream processes easier and more economic. These molecules can be extracted from fermentation broth and polymerized to produce a variety of biopolymers, e.g., polybutylene terephthalate, polyethylene terephthalate, polytrimethylene terephthalate, nylon-5,4 and nylon-4,6, with applications in medicine, pharmaceuticals, and textiles. Microbes are unable to naturally produce these types of polymers; thus, the production of building blocks and their polymerization is a fascinating approach for the production of these polymers. In comparison to naturally occurring biopolymers, synthesized polymers have improved and controlled structures and higher purity. The production of monomer units provides a new direction for polymer science because new classes of polymers with unique properties that were not previously possible can be prepared. Furthermore, the engineering of microbes for building-block production is an easy process compared to engineering an entire biopolymer synthesis pathway in a single microbe. Polyesters and polyamide polymers have become an important part of human life, and their demand is increasing daily. In this review, recent approaches and technology are discussed for the production of polyester/polyamide building blocks, i.e., 2-hydroxyisobutyric acid, 3-hydroxypropionic acid, mandelic acid, itaconic acid, adipic acid, terephthalic acid, succinic acid, 1,3-propanediol, 2,3-butanediol, 1,4-butanediol, 1,3-butanediol, cadaverine, and putrescine. 相似文献
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Due to increasing concerns about environmental problems, climate change and limited fossil resources, bio-based production of chemicals and polymers is gaining attention as one of the solutions to these problems. Polyhydroxyalkanoates (PHAs) are polyesters that can be produced by microbial fermentation. PHAs are synthesized using monomer precursors provided from diverse metabolic pathways and are accumulated as distinct granules inside the cells. On the other hand, most so-called bio-based polymers including polybutylene succinate, polytrimethylene terephthalate, and polylactic acid (PLA) are synthesized by a chemical process using monomers produced by fermentation. PLA, an attractive biomass-derived plastic, is currently synthesized by heavy metal-catalyzed ring opening polymerization of L-lactide that is made from fermentation-derived L-lactic acid. Recently, a complete biological process for the production of PLA and PLA copolymers from renewable resources has been developed by direct fermentation of recombinant bacteria employing PHA biosynthetic pathways coupled with a novel metabolic pathway. This could be accomplished by establishing a pathway for generating lactyl-CoA and engineering PHA synthase to accept lactyl-CoA as a substrate combined with systems metabolic engineering. In this article, we review recent advances in the production of lactate-containing homo- and co-polyesters. Challenges remaining to efficiently produce PLA and its copolymers and strategies to overcome these challenges through metabolic engineering combined with enzyme engineering are discussed. 相似文献
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Atul K. Singh B. M. Tripathi Harmesh Sahay R. N. Singh Rajeev Kaushik A. K. Saxena D. K. Arora 《Indian journal of microbiology》2010,50(1):2-11
1,2-Propanediol (propylene glycol) is an existing commodity chemical and can be produced from renewable resources using microbes. By virtue of being a natural product, relevant biochemical pathways can be harnessed into fermentation processes to produce 1,2-propanediol. In the present review, the chemical process and different biological strategies for the production of 1,2-propanediol are reviewed and compared with the potentials and limitations of all processes. For the successful commercial production of this diol, it is necessary to establish the metabolic pathways and production hosts (microorganisms), which are capable of delivering final product with high yields and volumetric productivity. Three pathways which have been recognized for 1,2-propanediol production are discussed here. In the first, de-oxy sugars like fucose and rhamnose are used as the carbon sources, while in the other route, the glycolytic intermediate-dihydroxyacetonephosphate (DHAP) is used to produce 1,2-propanediol via the formation of methylglyoxal. A new pathway of 1,2-propanediol production by lactic acid degradation under anoxic conditions and the enzymes involved is also discussed. The production of this diol has gained attention because of their newer applications in industries such as polymers, food, pharmaceuticals, textiles, etc. Furthermore, improvement in fermentation technology will permit its uses in other applications. Future prospect in the light of the current research and its potential as a major bulk chemical are discussed. 相似文献
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Eberl A Heumann S Kotek R Kaufmann F Mitsche S Cavaco-Paulo A Gübitz GM 《Journal of biotechnology》2008,135(1):45-51
Oligomers and polymers (film, fabrics) of the linear aromatic polyester poly(trimethylene terephthalate) (PTT) were treated with polyesterases from Thermomyces lanuginosus, Penicillium citrinum, Thermobifida fusca and Fusarium solani pisi. The cutinase from T. fusca was found to release the highest amounts of hydrolysis products from PTT materials and was able to open and hydrolyse a cyclic PTT dimer according to RP-HPLC–UV detection. In contrast, the lipase from T. lanuginosus also showed activity on the PTT fibres and on bis(3-hydroxypropyl) terephthalate (BHPT) but was not able to hydrolyse the polymer film, mono(3-hydroxypropyl) terephthalate (MHPT) nor the cyclic dimer of PTT. As control enzymes inhibited with mercury chloride were used. Surface hydrophilicity changes were investigated with contact angle measurements and the degree of crystallinity changes were determined with DSC. 相似文献
7.
Aims: The feasibility of the continuous production of a valuable bioplastic raw material, namely 1,3‐propanediol (1,3‐PDO) from biodiesel by‐product glycerol, using immobilized cells was investigated. In addition, the effect of hydraulic retention time (HRT) was also analysed. Methods and Results: Ceramic balls and ceramic rings were used for the immobilization of a locally isolated strain; Klebsiella pneumoniae (GenBank no. 27F HM063413 ). HRT of 1 h is the best one in terms of volumetric production rate (g 1,3‐PDO l?1 h?1). The results indicated that ceramic‐based cell immobilization achieved a 2‐fold higher production rate (10 g 1,3‐PDO l?1 h?1) in comparison with suspended cell system (4·9 g 1,3‐PDO l?1 h?1). Conclusions: Continuous cultures with immobilized cells revealed that 1,3‐PDO production was more effective and more stable than suspended culture systems. Furthermore, cell immobilization had also obvious benefits especially for resistance of the production for extreme conditions (high organic loading rates, cell washouts). The results were important for understanding the significance of continuous immobilization process among other well‐known 1,3‐PDO fermentation processes. Significance and Impact of the Study: This work is a promising process for further studies, as the immobilized micro‐organism was able to reach high volumetric production rates at short HRT, it has an important role in tolerating and converting glycerol during fermentation. Therefore, HRT is a very significant operational parameter (P value <0·05) directly affecting the bioreactor performance and production rate. 相似文献
8.
Richa Bafana 《Critical reviews in biotechnology》2018,38(1):68-82
Currently, growing attention is being devoted to the conversion of biomass into value-added products, such as itaconic acid (IA), which is considered as the cleanest alternative to petroleum-based acrylic acid. IA is an unsaturated dicarboxylic acid that is used as a building block chemical for the production of several value-added products such as poly-itaconic acid. IA and its derivatives have a wide range of potential applications in textile, paint, pharmaceutical and chemical industries. Presently, industries are producing IA on the large scale by fermentation from glucose. However, due to the primary utility of glucose as a food, it cannot meet the global demand for IA production in an economical way. The main challenge, so far, has been the production technology, which does not support cost-effective and competitive production of IA. This review discusses the various bottlenecks faced during each step of IA production, along with possible remedies to deal with these problems. Furthermore, it reviews the recent progress in fermentative IA production and sheds light on different microorganisms used, potential substrates and fermentation conditions. The review also covers market potential for IA, which indicates that IA can be produced cost-effectively from sustainable substrates, and it has the potential to replace petrochemicals in the near future. 相似文献
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The development of technologies for poly(ethylene terephthalate) (PET) depolymerization, such as biocatalysis, has been pointed as a very promising alternative to chemical hydrolysis processes. This work aims to understand the behavior of Yarrowia lipolytica, a robust yeast for diverse applications, in the presence of molecules from the PET production chain such as monoethylene glycol (MEG), terephthalic acid (TPA), bis (2-hydroxyethyl) terephthalate (BHET), PET oligomers, amorphous PET and post-consumer PET. The yeast was cultivated in rich media with and without glucose addition, in order to compare monomers release or consumption. TPA and MEG were consumed more intensely in the absence of glucose. The addition of the diester BHET yielded a 3-fold increased lipase production both at 160 rpm (118 U/L) and 250 rpm (385 U/L). In addition, 250 rpm agitation also provided a higher consumption of TPA (26% increase). The mono(2-hydroxyethyl) terephthalate (MHET) was the main intermediate released during polymer hydrolysis, followed by TPA and BHET. Thus, the use of Yarrowia lipolytica, which is capable of catalyzing the PET hydrolysis is of great potential to reduce the environmental impacts caused by unappropriated disposal of packages. 相似文献
10.
Yujun Zhang Chengwei Ma Wanda Dischert Philippe Soucaille An‐Ping Zeng 《Biotechnology journal》2019,14(9)
Phosphoserine aminotransferase (SerC) from Escherichia coli (E. coli) MG1655 is engineered to catalyze the deamination of homoserine to 4‐hydroxy‐2‐ketobutyrate, a key reaction in producing 1,3‐propanediol (1,3‐PDO) from glucose in a novel glycerol‐independent metabolic pathway. To this end, a computation‐based rational approach is used to change the substrate specificity of SerC from l ‐phosphoserine to l ‐homoserine. In this approach, molecular dynamics simulations and virtual screening are combined to predict mutation sites. The enzyme activity of the best mutant, SerCR42W/R77W, is successfully improved by 4.2‐fold in comparison to the wild type when l ‐homoserine is used as the substrate, while its activity toward the natural substrate l ‐phosphoserine is completely deactivated. To validate the effects of the mutant on 1,3‐PDO production, the “homoserine to 1,3‐PDO” pathway is constructed in E. coli by coexpression of SerCR42W/R77W with pyruvate decarboxylase and alcohol dehydrogenase. The resulting mutant strain achieves the production of 3.03 g L?1 1,3‐PDO in fed‐batch fermentation, which is 13‐fold higher than the wild‐type strain and represents an important step forward to realize the promise of the glycerol‐independent synthetic pathway for 1,3‐PDO production from glucose. 相似文献
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Edit Hirsch Hajnalka Pataki Júlia Domján Attila Farkas Panna Vass Csaba Fehér Zsolt Barta Zsombor K. Nagy György J. Marosi István Csontos 《Biotechnology progress》2019,35(5):e2848
Raman spectroscopy as a process analytical technology tool was implemented for the monitoring and control of ethanol fermentation carried out with Saccharomyces cerevisiae. The need for the optimization of bioprocesses such as ethanol production, to increase product yield, enhanced the development of control strategies. The control system developed by the authors utilized noninvasive Raman measurements to avoid possible sterilization problems. Real-time data analysis was applied using partial least squares regression (PLS) method. With the aid of spectral pretreatment and multivariate data analysis, the monitoring of glucose and ethanol concentration was successful during yeast fermentation with the prediction error of 4.42 g/L for glucose and 2.40 g/L for ethanol. By Raman spectroscopy-based feedback control, the glucose concentration was maintained at 100 g/L by the automatic feeding of concentrated glucose solution. The control of glucose concentration during fed-batch fermentation resulted in increased ethanol production. Ethanol yield of 86% was achieved compared to the batch fermentation when 75 % yield was obtained. The results show that the use of Raman spectroscopy for the monitoring and control of yeast fermentation is a promising way to enhance process understanding and achieve consistently high production yield. 相似文献
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This paper presents a review of the existing fermentation processes for the production of medium-chain-length poly-3-hydroxyalkanoates
(MCL-PHAs). These biodegradable polymers are usually produced most efficiently from structurally related carbon sources such
as alkanes and alkanoic acids. Unlike alkanoic acids, alkanes exhibit little toxicity but their low aqueous solubility limits
their use in high density culture. Alkanoic acids pose little mass transfer difficulty, but their toxicity requires that their
concentration be well controlled. Using presently available technology, large-scale production of MCL-PHA from octane has
been reported to cost from US $5 to 10 per kilogram, with expenditures almost evenly divided between carbon source, fermentation
process, and the separation process. However, MCL-PHAs, even some with functional groups in their subunits, can also be produced
from cheaper unrelated carbon sources, such as glucose. Metabolic engineering and other approaches should also allow increased
PHA cellular content to be achieved. These approaches, as well as a better understanding of fermentation kinetics, will likely
result in increased productivity and lower production costs. 相似文献
13.
3-Hydroxypropionaldehyde (3-HPA), an important intermediary metabolite of 1,3-propanediol (PDO) production, would be toxic to the cell growth and led to the abnormal cessation of the fermentation process. In this study, the dhaD gene encoding glycerol dehydrogenase (GDH) and dhaT gene encoding 1,3-propanediol oxidoreductase (PDOR) were overexpressed in Klebsiella pneumoniae ACCC 10082 to decrease the 3-HPA accumulation and increase the coenzyme NADH supply. By the construction of pTD plasmid, GDH and PDOR were both overexpressed and their enzyme activities were increased by 2.6- and 3.2-fold, respectively. The enzyme activity ratio of PDOR/GDHt (glycerol dehydratase) also was increased. On the other hand, NADH production was enhanced and the ratio of NADH/NAD+ exceeded 1 after the inducement of IPTG for the constructed strain. The two factors enhanced the transformation of 3-HPA to PDO. In the batch and fed-batch fermentation by the constructed strain, the peak of 3-HPA accumulation reduced by 52.2% and 33.3%, respectively, compared with the control. The PDO concentration and yield reached 59.2 g/L and 0.48 mol/mol, respectively. Furthermore, the fed-batch fermentation process appeared easier to be regulated. This work is considered helpful for the further understanding on the PDO metabolic mechanism of K. pneumoniae and also useful for the PDO fermentation in a large-scale bioreactor. 相似文献
14.
利用废弃物发酵法生产聚羟基烷酸PHAs 总被引:1,自引:0,他引:1
聚羟基烷酸(PHAs)是一种可降解聚合物,与石化塑料相比它具有生物降解性及生物相容性等优点,在不久的将来必然有广阔的应用前景。生产PHAs的主要方法是发酵法,在过去的几十年里传统的深层发酵法生产PHAs的工艺已经得到深入的研究,近些年固态发酵法生产PHAs也吸引了越来越多研究者的关注。 相似文献
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Biotechnological production of enantiomeric pure lactic acid from renewable resources: recent achievements, perspectives, and limits 总被引:1,自引:0,他引:1
Kenji Okano Tsutomu Tanaka Chiaki Ogino Hideki Fukuda Akihiko Kondo 《Applied microbiology and biotechnology》2010,85(3):413-423
Lactic acid (LA) is an important and versatile chemical that can be produced from renewable resources such as biomass. LA
is used in the food, pharmaceutical, and polymers industries and is produced by microorganism fermentation; however, most
microorganisms cannot directly utilize biomass such as starchy materials and cellulose. Here, we summarize LA production using
several kinds of genetically modified microorganisms, such as LA bacteria, Escherichia coli, Corynebacterium glutamicum, and yeast. Using gene manipulation and metabolic engineering, the yield and optical purity of LA produced from biomass has
been significantly improved. In this review, the drawbacks as well as improvements of LA production by fermentation is discussed. 相似文献
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Emerging biotechnologies for production of itaconic acid and its applications as a platform chemical
Recently, itaconic acid (IA), an unsaturated C5-dicarboxylic acid, has attracted much attention as a biobased building block chemical. It is produced industrially (>80 g L?1) from glucose by fermentation with Aspergillus terreus. The titer is low compared with citric acid production (>200 g L?1). This review summarizes the latest progress on enhancing the yield and productivity of IA production. IA biosynthesis involves the decarboxylation of the TCA cycle intermediate cis-aconitate through the action of cis-aconitate decarboxylase (CAD) enzyme encoded by the CadA gene in A. terreus. A number of recombinant microorganisms have been developed in an effort to overproduce it. IA is used as a monomer for production of superabsorbent polymer, resins, plastics, paints, and synthetic fibers. Its applications as a platform chemical are highlighted. It has a strong potential to replace petroleum-based methylacrylic acid in industry which will create a huge market for IA. 相似文献
19.
Chen Y 《Journal of industrial microbiology & biotechnology》2011,38(5):581-597
This article reviews current co-culture systems for fermenting mixtures of glucose and xylose to ethanol. Thirty-five co-culture
systems that ferment either synthetic glucose and xylose mixture or various biomass hydrolysates are examined. Strain combinations,
fermentation modes and conditions, and fermentation performance for these co-culture systems are compared and discussed. It
is noted that the combination of Pichia stipitis with Saccharomyces cerevisiae or its respiratory-deficient mutant is most commonly used. One of the best results for fermentation of glucose and xylose
mixture is achieved by using co-culture of immobilized Zymomonas mobilis and free cells of P. stipitis, giving volumetric ethanol production of 1.277 g/l/h and ethanol yield of 0.49–0.50 g/g. The review discloses that, as a
strategy for efficient conversion of glucose and xylose, co-culture fermentation for ethanol production from lignocellulosic
biomass can increase ethanol yield and production rate, shorten fermentation time, and reduce process costs, and it is a promising
technology although immature. 相似文献
20.
Restructuring and optimization of the conventional fermentation industry for fuel and chemical production is necessary to replace petrochemical production routes. Guided by this concept, a novel biorefinery process has been developed as an alternative to conventional upstream processing routes, leading to the production of a generic fermentation feedstock from wheat. The robustness of Aspergillus awamori as enzyme producer is exploited in a continuous fungal fermentation on whole wheat flour. Vital gluten is extracted as an added-value byproduct by the conventional Martin process from a fraction of the overall wheat used. Enzymatic hydrolysis of gluten-free flour by the enzyme complex produced by A. awamori during fermentation produces a liquid stream rich in glucose (320 g/L). Autolysis of fungal cells produces a micronutrient-rich solution similar to yeast extract (1.6 g/L nitrogen, 0.5 g/L phosphorus). The case-specific combination of these two liquid streams can provide a nutrient-complete fermentation medium for a spectrum of microbial bioconversions for the production of such chemicals as organic acids, amino acids, bioethanol, glycerol, solvents, and microbial biodegradable plastics. Preliminary economic analysis has shown that the operating cost required to produce the feedstock is dependent on the plant capacity, cereal market price, presence and market value of added-value byproducts, labor costs, and mode of processing (batch or continuous). Integration of this process in an existing fermentation plant could lead to the production of a generic feedstock at an operating cost lower than the market price of glucose syrup (90% to 99% glucose) in the EU, provided that the plant capacity exceeds 410 m(3)/day. Further process improvements are also suggested. 相似文献