One-step synthesis of 12-ketoursodeoxycholic acid from dehydrocholic acid using a multienzymatic system

12-ketoursodeoxycholic acid (12-keto-UDCA) is a key intermediate for the synthesis of ursodeoxycholic acid (UDCA), an important therapeutic agent for non-surgical treatment of human cholesterol gallstones and various liver diseases. The goal of this study is to develop a new enzymatic route for the synthesis 12-keto-UDCA based on a combination of NADPH-dependent 7β-hydroxysteroid dehydrogenase (7β-HSDH, EC 1.1.1.201) and NADH-dependent 3α-hydroxysteroid dehydrogenase (3α-HSDH, EC 1.1.1.50). In the presence of NADPH and NADH, the combination of these enzymes has the capacity to reduce the 3-carbonyl- and 7-carbonyl-groups of dehydrocholic acid (DHCA), forming 12-keto-UDCA in a single step. For cofactor regeneration, an engineered formate dehydrogenase, which is able to regenerate NADPH and NADH simultaneously, was used. All three enzymes were overexpressed in an engineered expression host Escherichia coli BL21(DE3)Δ7α-HSDH devoid of 7α-hydroxysteroid dehydrogenase, an enzyme indigenous to E. coli, in order to avoid formation of the undesired by-product 12-chenodeoxycholic acid in the reaction mixture. The stability of enzymes and reaction conditions such as pH value and substrate concentration were evaluated. No significant loss of activity was observed after 5 days under reaction condition. Under the optimal condition (10 mM of DHCA and pH 6), 99 % formation of 12-keto-UDCA with 91 % yield was observed.     

Enzymatic reduction of dehydrocholic acid to 12-ketochenodeoxycholic acid with NADH regeneration

12-Ketochenodeoxycholic acid, an essential intermediate in the synthesis of chenodeoxycholic acid, has been enzymatically prepared from dehydrocholic acid. The specific reduction of dehydrocholic with NADH was catalysed by 3α-hydroxysteroid dehydrogenase (3α-hydroxysteroid: NAD(P)⁺ oxidoreductase, EC 1.1.1.50) and 7α-hydroxysteroid dehydrogenase (7α-hydroxysteroid:NAD⁺ 7-oxidoreductase, EC 1.1.1.159). Cofactor regeneration was obtained through the formate dehydrogenase (formate:NAD⁺ oxidoreductase, EC 1.2.1.2) catalysed oxidation of formate. Complete transformation of dehydrocholic acid to the 12-keto derivative was achieved with a coenzyme turnover number up to 1200. No steroid by-products were detected by high performance liquid chromatography and thin layer chromatography. The process yielded 9 g product l^?1 in 66–84 h. The high purity of the enzymatically prepared 12-ketochenodeoxycholic acid should drastically reduce the formation of the toxic by-product lithocholic acid, which occurs in the synthesis of chenodeoxycholic acid when using chemical methods alone.     

A new enzymatic route to the synthesis of 12-ketoursodeoxycholic acid

Summary Cholic acid (3,7,12-trihydroxy-5-cholanoic acid) was completely and selectively transformed into 12-ketoursodeoxycholic acid (3,7-dihydroxy-12-oxo-5-cholanoic acid) by means of two consecutive enzymatic steps catalyzed, the first, by 7- and 12-hydroxysteroid dehydrogenase and, the second, by 7-hydroxysteroid dehydrogenase. Coenzyme regeneration was carried out with -ketoglutarate-glutamate dehydrogenase and glucose-glucose dehydrogenase, respectively.     

Microbial production of chenodeoxycholic acid precursor, 12-ketochenodeoxycholic acid,from dehydrocholic acid

Summary Two kinds of bacteria (DC33 and DC1115) were isolated from soil as biotransformers of dehydrocholic acid to 12-ketochenodeoxycholic acid, and identified to be Brevibacterium fuscum and Lactobacillus xylosus, respectively. Dehydrocholic acid was converted via 7,12-diketolithocholic acid to 12-ketochenodeoxycholic acid by both strains, and the product and the intermediate were isolated and chemically identified. By using a jar fermentor, 12-ketochenodeoxycholic acid was produced with a more than 50% yield after 52 h by Brevibacterium fuscum with aerobic growth and anaerobic conversion, and after 24 h by Lactobacillus xylosus under anaerobic conditions, respectively.     

Enzymatic synthesis of D-glucosaminic acid from D-glucosamine

D-glucosaminic acid (2-amino-2-deoxy-D-gluconic acid), a component of bacterial lipopolysaccharides and a chiral synthon, is easily prepared on a multigram scale by air oxidation of D-glucosamine (2-amino-2-deoxy-D-glucose) catalysed by glucose oxidase.     

Enzymatic protein hydrolysis in a membrane reactor related to taste properties

Potato, Vicia faba and soybean proteins were hydrolysed enzymatically in a substrate feed membrane reactor system. Alkaline proteolytic enzymes and PM-10 membranes were used for the hydrolysis of potato protein. The taste of the ultrafiltrates, which was unpleasantly bitter and potato-like, was improved by application of gelatin. Also using PM-10 membranes, Vicia faba protein isolate was hydrolysed by alkaline and acid proteolytic enzymes. The bitterness of the ultrafiltrate decreased with the formation of an isoelectric precipitate, which was probably due to association of hydrophobic peptides. The reactor equipped with a cellulose acetate membrane delivered an acceptable enzymatic hydrolysate of Promine D during the first hours of ultrafiltration. This was not the case when similar processes were performed using non-cellulosic DM-5 membranes. The usefulness of ultrafiltration for obtaining bland protein hydrolysates seems to be limited to short-term processes with cellulose acetate membranes.     

Enzymatic hydrolysis of sodium-hydroxide-pretreated sallow in an ultrafiltration membrane reactor

An ultrafiltration membrane reactor was used to investigate the recovery of biocatalysts during enzymatic hydrolysis of pretreated sallow. Product inhibition could be eliminated by continuous removal of products through the ultrafiltration membrane, thus retaining the macromolecular substrate and enzymes. In this way, the degree of conversion was improved from 40% in a batch hydrolysis to 95% (within 20 h), and the initial hydrolysis rate was increased up to seven times. The recovery studies were focused on mechanical deactivation and irreversible adsorption on to the nonconvertible fraction of the substrate. Cellulase deactivation during mechanical agitation was not significant, and the loss of activity was attributed mainly to strong adsorption of the enzymes onto undigested material. This process was studied in semicontinuous hydrolyses, where fresh substrate was added intermittently. The amount of reducing sugars produced in this experiment was 25.7 g/g enzyme, compared to 4.7 g/g enzyme in a batch hydrolysis.     

Enzymatic synthesis of ascorbyl ester derived from linoleic acid

Bioprocess and Biosystems Engineering - Antioxidants are substances that defend cells against damage, kidnapping and destroying free radicals. They have been largely used in the food industry due...     

Dipeptide synthesis and separation in a reversed micellar membrane reactor

The synthesis of dipeptide AcPheLeuNH₂ catalyzed by α-chymotrypsin encapsulated in TTAB/octanol/heptane reversed micelles was investigated in a tubular ceramic membrane reactor, operated in a batch mode. The reaction medium conditions (TTAB concentration, buffer molarity, and pH) were optimized using a factorial design in order to achieve maximum synthesis rates. Hydrated reversed micelles permeated through the membrane together with the substrate ester, dipeptide, and by-products. However, as a result of the low solubility of the peptide in the reaction medium, selective precipitation occurred, thus enabling the complete retention of the solid product by the ultrafiltration membrane and therefore an integration of a separation step in the biotransformation process. In spite of the continuous accumulation of solids inside the reactor, constant permeation flow rates could be maintained throughout the operation. The influence of α-chymotrypsin, TTAB, and water concentration on the kinetics and mass transfer of the system was also investigated. The behavior of the system during a continuous experiment was also evaluated.     

Enzymatic hydrolysis of sodium caseinate in a continuous ultrafiltration reactor using an inorganic membrane

Continuous hydrolysis of sodium caseinate by alcalase was investigated in a recycle bioreactor coupled to an inorganic M5 membrane module. The effects of various substrate concentrations and the role of an ultrafiltration membrane on conversion rate were reported. Although a high level of conversion was obtained in the retentate side at a steady state, only part of the products formed was transmitted through the inorganic membrane. Degree of hydrolysis and product concentration in the reactor seem to be the main factors limiting product output during the continuous hydrolysis.     

Enzymatic cleaning of biofouled thin-film composite reverse osmosis (RO) membrane operated in a biofilm membrane reactor

Application of environmentally friendly enzymes to remove thin-film composite (TFC) reverse osmosis (RO) membrane biofoulants without changing the physico-chemical properties of the RO surface is a challenging and new concept. Eight enzymes from Novozyme A/S were tested using a commercially available biofouling-resistant TFC polyamide RO membrane (BW30, FilmTech Corporation, Dow Chemical Co.) without filtration in a rotating disk reactor system operated for 58 days. At the end of the operation, the accumulated biofoulants on the TFC RO surfaces were treated with the three best enzymes, Subtilisin protease and lipase; dextranase; and polygalacturonase (PG) based enzymes, at neutral pH (~7) and doses of 50, 100, and 150 ppm. Contact times were 18 and 36 h. Live/dead staining, epifluorescence microscopy measurements, and 5 μm thick cryo-sections of enzyme and physically treated biofouled membranes revealed that Subtilisin protease- and lipase-based enzymes at 100 ppm and 18 h contact time were optimal for removing most of the cells and proteins from the RO surface. Culturable cells inside the biofilm declined by more than five logs even at the lower dose (50 ppm) and shorter incubation period (18 h). Subtilisin protease- and lipase-based enzyme cleaning at 100 ppm and for 18 h contact time restored the hydrophobicity of the TFC RO surface to its virgin condition while physical cleaning alone resulted in a 50° increase in hydrophobicity. Moreover, at this optimum working condition, the Subtilisin protease- and lipase-based enzyme treatment of biofouled RO surface also restored the surface roughness measured with atomic force microscopy and the mass percentage of the chemical compositions on the TFC surface estimated with X-ray photoelectron spectroscopy to its virgin condition. This novel study will encourage the further development and application of enzymes to remove biofoulants on the RO surface without changing its surface properties.