Department of Biochemistry, Research Center, Denki Kagaku Kogyo Co., Ltd., 3-5-1 Asahimachi, Machida-shi, Tokyo 194, Japan.
Biotechnol Bioeng. 1990 Jun 20;36(2):149-54. doi: 10.1002/bit.260360207.
The concept of a charged membrane bioreactor (CMBR) has been proposed for continuous reactions of enzymatic reduction dependent upon the nicotinamide coenzyme NADP(H). It was found that a composite membrane with a negative charge, NTR 7410, could retain NADP(H) selectively without any chemical modification. Several permeation experiments have revealed that the retainment of a coenzyme is based on electrostatic repulsion of negative charges between the membrane and the phosphate moiety of NADP(H). The retainment ratio was reduced by the addition of inorganic salt, although it could be restored to 0.8 in the presence of albumin. A reactor equipped with a charged membrane as the coenzyme separator module was constructed and used in the continuous production of sorbitol. NADPH-dependent aldose reductase isolated from Candida tropicalis IAM 12202 was used for the production of sorbitol from glucose. The coenzyme oxidized in this reaction was enzymatically regenerated by conjugation with glucose dehydrogenase, together with the coproduction of gluconic acid from glucose. With a substrate conversion of 85%, 100 g/L sorbitol was produced and equimolar gluconic acid was coproduced for more than 800 h, indicating that the reaction was efficiently coupled to the enzymatic regeneration. The initial high retainment ratio of the membrane was almost maintained throughout the entire reaction. Consequently, the turnover number of the coenzyme reached 106,000.
已提出带电荷膜生物反应器(CMBR)的概念,用于依赖烟酰胺辅酶 NADP(H)的酶促还原的连续反应。发现具有负电荷的复合膜 NTR 7410 无需任何化学修饰即可选择性地保留 NADP(H)。几项渗透实验表明,辅酶的保留基于膜和 NADP(H)的磷酸部分之间的负电荷之间的静电排斥。尽管在白蛋白存在下可以将保留率恢复至 0.8,但添加无机盐会降低保留率。构建了配备带电荷膜作为辅酶分离模块的反应器,并用于连续生产山梨糖醇。使用从热带假丝酵母 IAM 12202 分离的 NADPH 依赖性醛糖还原酶将葡萄糖转化为山梨糖醇。在该反应中氧化的辅酶通过与葡萄糖脱氢酶缀合而酶促再生,同时从葡萄糖共生产葡萄糖酸。在底物转化率为 85%的情况下,生产了 100 g/L 的山梨糖醇,共生产了等摩尔的葡萄糖酸,持续了 800 多个小时,表明该反应与酶促再生有效地偶联。膜的初始高保留率在整个反应过程中几乎保持不变。因此,辅酶的周转率达到 106000。