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利用甘蔗伯克霍尔德氏菌调控聚(3-羟基丁酸-co-4-羟基丁酸)单体组成和生产效率的喂养策略。

Feeding strategies for tuning poly (3-hydroxybutyrate-co-4-hydroxybutyrate) monomeric composition and productivity using Burkholderia sacchari.

机构信息

iBB-Institute for Bioengineering and Biosciences, Bioengineering Department, Instituto Superior Técnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal.

iBB-Institute for Bioengineering and Biosciences, Bioengineering Department, Instituto Superior Técnico, Av. Rovisco Pais, 1049-001 Lisboa, Portugal; CiiEM-Centro de Investigação Interdisciplinar Egas Moniz, Instituto Superior de Ciências da Saúde Egas Moniz, Campus Universitário, Quinta da Granja, 2829-511 Monte de Caparica, Portugal.

出版信息

Int J Biol Macromol. 2017 Dec;105(Pt 1):825-833. doi: 10.1016/j.ijbiomac.2017.07.111. Epub 2017 Jul 19.

Abstract

Poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P(3HB-4HB)) co-polymers were produced at bench-scale in fed-batch cultivations by Burkholderia sacchari from glucose (main carbon-source) and gamma-butyrolactone (GBL) as co-substrate. As P(3HB-4HB) properties highly depend on the 4-hydroxybutyrate (4HB) molar fraction, it is advantageous to have a thorough knowledge of the process in order to promote the production of the targeted final product. In this work, polymers with a 4HB molar percentage ranging from 1.5 to 8.4% (mol/mol) were obtained as consequence of a fine tuning of the fed-batch operation conditions, namely regarding the co-substrate feeding rate and its addition time, as GBL is toxic to B. sacchari cells. The best results regarding both the 4HB incorporation (molar%) and the co-polymer productivity (7.1% and 1.1g/(L.h) respectively) were reached when a pulse of GBL (<10g/L) was added early in the accumulation phase followed by a constant GBL addition at a rate similar to that of consumption so that a steady co-substrate concentration in the medium was maintained.

摘要

聚(3-羟基丁酸-co-4-羟基丁酸)(P(3HB-4HB))共聚物由糖(主要碳源)和γ-丁内酯(GBL)作为共底物在毕赤酵母的分批补料培养中在实验室规模下生产。由于 P(3HB-4HB)的性质高度依赖于 4-羟基丁酸(4HB)的摩尔分数,因此深入了解该过程有利于促进目标最终产物的生产。在这项工作中,通过精细调整分批补料操作条件,获得了摩尔百分比为 1.5%至 8.4%(摩尔/摩尔)的聚合物,即共底物进料速率及其添加时间,因为 GBL 对 B. sacchari 细胞有毒。当在积累阶段早期添加少量 GBL(<10g/L),然后以与消耗速率相似的速率恒定添加 GBL,从而保持培养基中稳定的共底物浓度时,共聚物的 4HB 掺入量(摩尔%)和共聚物生产力(分别为 7.1%和 1.1g/(L.h))达到最佳。

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