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异丁烯的发酵生产。

Fermentative production of isobutene.

机构信息

Department of Biotechnology, Delft University of Technology, Delft, The Netherlands.

出版信息

Appl Microbiol Biotechnol. 2012 Feb;93(4):1377-87. doi: 10.1007/s00253-011-3853-7. Epub 2012 Jan 11.

DOI:10.1007/s00253-011-3853-7
PMID:22234536
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC3275743/
Abstract

Isobutene (2-methylpropene) is one of those chemicals for which bio-based production might replace the petrochemical production in the future. Currently, more than 10 million metric tons of isobutene are produced on a yearly basis. Even though bio-based production might also be achieved through chemocatalytic or thermochemical methods, this review focuses on fermentative routes from sugars. Although biological isobutene formation is known since the 1970s, extensive metabolic engineering is required to achieve economically viable yields and productivities. Two recent metabolic engineering developments may enable anaerobic production close to the theoretical stoichiometry of 1isobutene + 2CO(2) + 2H(2)O per mol of glucose. One relies on the conversion of 3-hydroxyisovalerate to isobutene as a side activity of mevalonate diphosphate decarboxylase and the other on isobutanol dehydration as a side activity of engineered oleate hydratase. The latter resembles the fermentative production of isobutanol followed by isobutanol recovery and chemocatalytic dehydration. The advantage of a completely biological route is that not isobutanol, but instead gaseous isobutene is recovered from the fermenter together with CO(2). The low aqueous solubility of isobutene might also minimize product toxicity to the microorganisms. Although developments are at their infancy, the potential of a large scale fermentative isobutene production process is assessed. The production costs estimate is 0.9 Euro kg(-1), which is reasonably competitive. About 70% of the production costs will be due to the costs of lignocellulose hydrolysate, which seems to be a preferred feedstock.

摘要

异丁烯(2-甲基丙烯)是一种化学物质,未来其生物基生产可能会取代石化生产。目前,每年异丁烯的产量超过 1000 万吨。尽管生物基生产也可以通过化学催化或热化学方法实现,但本综述重点介绍了从糖发酵的途径。尽管生物合成异丁烯的方法自 20 世纪 70 年代就已为人所知,但需要进行广泛的代谢工程才能实现经济上可行的产量和生产力。最近的两项代谢工程进展可能使厌氧生产接近每摩尔葡萄糖理论得率的 1 异丁烯+2CO2+2H2O。一种方法依赖于将 3-羟基异戊酸转化为异丁烯作为甲羟戊酸二磷酸脱羧酶的副产物,另一种方法依赖于异丁醇脱水作为工程化油酸水解酶的副产物。后一种方法类似于发酵生产异丁醇,然后回收异丁醇并进行化学催化脱水。完全生物途径的优势在于,与从发酵罐中回收异丁醇和 CO2 一起,从发酵罐中回收的是气态异丁烯,而不是异丁醇。异丁烯的低水溶解度也可能最小化产物对微生物的毒性。尽管发展仍处于起步阶段,但评估了大规模发酵异丁烯生产工艺的潜力。生产成本估计为 0.9 欧元/千克,具有相当的竞争力。大约 70%的生产成本将归因于木质纤维素水解物的成本,木质纤维素水解物似乎是一种首选的原料。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/ca8c9a9ea7c3/253_2011_3853_Fig6_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/2bc00d442f71/253_2011_3853_Fig1_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/ffbaabc40255/253_2011_3853_Fig2_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/c0ed8caea654/253_2011_3853_Fig3_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/864cf00d3c68/253_2011_3853_Fig4_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/9d292d230984/253_2011_3853_Fig5_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/ca8c9a9ea7c3/253_2011_3853_Fig6_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/2bc00d442f71/253_2011_3853_Fig1_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/ffbaabc40255/253_2011_3853_Fig2_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/c0ed8caea654/253_2011_3853_Fig3_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/864cf00d3c68/253_2011_3853_Fig4_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/9d292d230984/253_2011_3853_Fig5_HTML.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/bd5c/3275743/ca8c9a9ea7c3/253_2011_3853_Fig6_HTML.jpg

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