Subtilisin-catalyzed transesterification in supercritical carbon dioxide

Summary Subtilisin Carlsberg was found to catalyze transesterification between N-acetyl-L-phenylalanine chloroethyl ester and ethanol in supercritical carbon dioxide. The effects of different temperatures and carbon dioxide/ethanol ratios on the reaction rate were investigated. A comparative study showed that enzymatic transesterification is faster in supercritical carbon dioxide than in anhydrous organic solvents.     

Extraction of squalene from yeast by supercritical carbon dioxide

Squalene produced under anaerobic conditions, by a strain of Torulaspora delbrueckii was extracted from the biomass using supercritical carbon dioxide. Minimum use of solvent, lower time of isolation and a higher selectivity of extraction merit use of supercritical fluid extraction (SFE) technique over solvent extraction of squalene, as optimized and reported previously. A maximum squalene yield of 11.12 g g^–1 (dry weight) of yeast cells was obtained at a temperature of 60 °C and pressure of 250–255 bar at a constant flow rate of 0.2l min^–1 of carbon dioxide. Lyophilization prior to SFE increased the squalene yield to 430.52 g g^–1 dry weight of yeast cells, an amount that is far greater than that obtained by (2:1) chloroform–methanol solvent extraction.     

超临界二氧化碳的四个应用方向

综述了超临界CO2的四个主要应用方向,即萃取、细胞破壁和微粒制造、反应溶剂以及SCCO2洗涤,着重总结了在烟草工业上的应用。对国内外的应用现状和应用前景给予了评述,并给出CO2温度、压力、密度的关系式。     

Synthesis of poly(L-lactide) and polyglycolide by ring-opening polymerization

This protocol describes the synthesis of poly(L-lactide) by ring-opening polymerization of L-lactide using tin(II) 2-ethylhexanoate catalyst as well as the synthesis of polyglycolide by ring-opening polymerization of glycolide. Ring-opening polymerization of cyclic diesters synthesized from alpha-hydroxycarboxylic acids gives high-molecular-weight polyester in high yield. Tin(II) 2-ethylhexanoate catalyst is the most common catalyst for ring-opening polymerization of diesters owing to its high reactivity and low toxicity. Purity of monomers and the amount of water and alcohol in the reaction system are significant factors for increasing molecular weight and conversion of polyesters. The molecular weight of the polyesters is also dependent on reaction temperature and reaction time. This protocol can be completed in 3 d for the synthesis of poly(L-lactide) and 2 d for the synthesis of polyglycolide.     

Enantioselective esterification of ibuprofen in supercritical carbon dioxide by immobilized lipase

The enantioselective esterification of racemic ibuprofen with n-propanol by immobilized Mucor miehel lipase in supercritical carbon dioxide was studied. The enantiomeric excess of the product (ee_p) was 70 % at 15...20 % conversion. The enantioselectivity was faintly affected by temperature and the concentration of ibuprofen and lipase. The optimum temperature was 45 °C. The initial reaction rate increased with pressure, but enantioselectivity was not affected by pressure changes. The reaction rates in supercritical carbon dioxide at optimized conditions and in n-hexane were similar.     

Unfolding of poly-L-glutamic acid by microbubbling of supercritical carbon dioxide

The conformational changes in alpha-helical poly-L-glutamic acid caused by microbubbling supercritical CO2 were investigated with circular dichroism spectra. After microbubbling using a micropore filter at 35 and 30 MPa for 30 min, alpha-helix content decreased to 37%, while without the filter it was 68%. The alpha-helix structure was significantly decomposed by a high density of CO2. No important changes were observed in heating, autoclaving, or pH-lowering.     

Enzymatic dipeptide synthesis by surfactant-coated alpha-chymotrypsin complexes in supercritical carbon dioxide

Enzymatic dipeptide synthesis by surfactant-coated alpha-chymotrypsin complexes was performed in supercritical CO(2) and liquid CO(2) at 308.2 and 333.2 K at pressures of 6.1 and 10.1 MPa. The enzymatic activity of coated alpha-chymotrypsin complexes for dipeptides synthesis at 10.1 MPa in supercritical CO(2) (SC-CO(2)) was higher than that in a liquid CO(2) and ethyl acetate solution at 6.1 MPa. The behavior of alpha-chymotrypsin in SC-CO(2) was similar to that in liquid ethyl acetate. And increasing the pressure and temperature increased the maximum conversion and the enzymatic reaction rate in SC-CO(2). Furthermore, the control of the water content in the reaction media had a dominant effect on the enzymatic activity. The maximum conversion for the dipeptide synthesis by the surfactant-coated alpha-chymotrypsin was obtained at 4% water content. The alpha-chymotrypsin complexes exhibited a higher enzymatic activity than native alpha-chymotrypsin in SC-CO(2). The nonionic surfactants l-glutamic acid dialkyl ester ribitol amide and sorbitan monostearate were more favored than the anionic surfactant sodium bis(2-ethylhexyl)sulfosuccinate.     

Starch hydrolysis using enzyme in supercritical carbon dioxide

Summary The enzymatic hydrolysis reaction with supercritical carbon dioxide(SC-CO₂) as a reaction medium to make glucose from starch was investigated. The reaction rate was enhanced at higher temperature and pressure, especially near the critical point of the CO₂. The -amylase and glucoamylase were found to be active in a SC-CO₂.     

Effective terminal sterilization using supercritical carbon dioxide

Gentle alternatives to existing sterilization methods are called for by rapid advances in biomedical technologies. Supercritical fluid technologies have found applications in a wide range of areas and have been explored for use in the inactivation of medical contaminants. In particular, supercritical CO(2) is appealing for sterilization due to the ease at which the supercritical state is attained, the non-reactive nature, and the ability to readily penetrate substrates. However, rapid inactivation of bacterial endospores has proven a barrier to the use of this technology for effective terminal sterilization. We report the development of a supercritical CO(2) based sterilization process capable of achieving rapid inactivation of bacterial endospores while in terminal packaging. Moreover, this process is gentle; as the morphology, ultrastructure, and protein profiles of inactivated microbes are maintained. These properties of the sterilization process suit it for possible use on a wide range of biomedical products including: materials derived from animal tissues, protein based therapies, and other sensitive medical products requiring gentle terminal sterilization.     

Extraction of indole alkaloids fromCatharanthus roseus by using supercritical carbon dioxide

Summary Indole alkaloids, particularly vindoline and catharanthine, were extracted from the leaves ofCatharanthus roseus by supercritical extraction with CO₂. The contents of vindoline and catharanthine in the extracts were determined by HPLC and identified by LC/MS. About 52 %(w/w) of the initial vindoline content, 1.5 mg vindoline/g dry wt leaves, was recovered after extracting this material for 10 h with the CO₂ flow rate of 400 ml/min at 40°C and 150 bar. Vindoline concentration in the extract was 67 %(w/w).     

Recovery of oil components of okara by ethanol-modified supercritical carbon dioxide extraction

Recovery of the oil components of okara by ethanol-modified supercritical carbon dioxide extraction was investigated at 40-80 degrees C temperature and 12-30 MPa pressure. In a typical run (holding period of 2 h, continuous flow extraction of 5 h), results indicated that the oil component could be best obtained with a recovery of 63.5% at relatively low temperature of 40 degrees C and mild pressure of 20 MPa in the presence of 10 mol% EtOH as entrainer. Based on gas chromatography-mass spectrometry (GC-MS) analysis, the extracts consisted mainly of fatty acids and phytosterols, and traces of decadienal. Folin-Ciocalteau estimates of total phenols showed that addition of EtOH as entrainer increased the yield and the amount of phenolic compounds in the extracts. The amounts of two primary soy isoflavones, genistein and daidzein, in the extracts also increased with increasing amount of EtOH.     

Inactivation of Alternaria brassicicola spores by supercritical carbon dioxide with ethanol entrainer

Supercritical carbon dioxide (SC-CO₂) was used to inactivate fungal spores of Alternaria brassicicola. The inactivation conditions were optimized using response surface methodology (RSM). When the SC-CO₂-entrainer (ethanol) system was applied to fungal spores, the treatment time required for the complete inactivation of fungal spores was substantially reduced.     

Sterilizing Bacillus pumilus spores using supercritical carbon dioxide

Supercritical carbon dioxide (SC CO(2)) has been evaluated as a new sterilization technology. Results are presented on killing of B. pumilus spores using SC CO(2) containing trace levels of additives. Complete killing was achieved with 200 part per million (ppm) hydrogen peroxide in SC CO(2) at 60 degrees C, 27.5 MPa. Addition of water to SC CO(2) resulted in greater than three-log killing, but this is insufficient to claim sterilization. Neither ethanol nor isopropanol when added to SC CO(2) affected killing.     

Enzymatic synthesis of peptide in acetonitrile/supercritical carbon dioxide

Summary The peptide synthesis from N-acetyl-L-tyrosine ethyl ester (Ac-Tyr-OEt) and amino acid amides was realized using -chymotrypsin (CT) in acetonitrile (MeCN) or acetonitrile/supercritical carbon dioxide (SCCO₂) containing small amounts of water. In both solvent systems there was an optimum water content for peptide synthesis, above which peptide hydrolysis became more important. After an incubation for 5 hours, the yields of the peptide was 64% in MeCN and 91% in MeCN/SCCO₂, respectively.     

Effect of moisture on enzymatic reaction in supercritical carbon dioxide

The continuous acidolysis of triolein and stearic acid was carried out by an immobilized lipase to elucidate the characteristics of supercritical carbon dioxide (SC-CO₂) as a reaction medium. At first, an effect of temperature and pressure on the water adsorption to the immobilized lipase in the SC-CO₂ was examined. Then, the continuous interesterification of triolein and stearic acid by the moist immobilized lipase was examined. The amount of water adsorption to the immobilized lipase in the supercritical carbon dioxide measured under the condition of a different temperature and pressure has been expressed by a correlation equation of Freundlich type by using relative water standardized with the solubility of water in each condition. Optimum operating conditions of the interesterification by immobilized lipase in the SC-CO₂ was 323 K, 16.9 MPa and adsorbed-water concentration of 2 wt%. The production rate obtained by enzymatic acidolysis in the SC-CO₂ was found to be about 0.03 mmol/h2g-immobilized enzyme, leaving 74% residual triglyceride at the optimum operating conditions.     

Preparation of peptide-loaded polymer microparticles using supercritical carbon dioxide

In this study, peptide-loaded microparticles were prepared using an aerosol solvent extraction system (ASES) by employing supercritical carbon dioxide as an antisolvent. The effects of the molecular weight of poly(Llactide) (PLLA), poly(ethylene glycol) (PEG), the block length of methoxy poly(ethylene glycol)-b-poly(L-lactide) (mPEG-PLLA), the blending of PLLA and PEG, and the drug-to-polymer feed ratio on the formation of leuprolide acetate (LA)-loaded microparticles and their release characteristics were investigated. Scanning electron microscope observations showed that the LA-loaded polymer particles had a spherical morphology with a smooth surface. The entrapment efficiency of LA in the ASES-processed microparticles was found to be extremely high (about 99%), whereas the initial release rate of the LA-loaded microparticles was very low for PLLA. The release rate of LA was observed to increase as the PEG block length of mPEG-PLLA and/or the drug content in the microparticles increased. When PLLA was blended with PEG, the release rate of LA from the PLLA/PEG microparticles was significantly faster compared with the corresponding mPEG-PLLA copolymer.     

Continuous reaction-separation process for enzymatic esterification in supercritical carbon dioxide

The study of enzymatic esterification by an immobilized lipase in supercritical carbon dioxide (SCCO(2)) and in n-hexane, described in our previous works, was extended to continuous operation in a tubular fixed bed. The modeling of the reaction vessel operation was achieved through the use of the simple plug flow model coupled with the appropriate kinetic equation. Comparison with experiments proved to be satisfactory. The study of the postreactional separation, an important feature when using SCCO(2), was undertaken experimentally and good selectivities and product recovery were obtained. (c) 1994 John Wiley & Sons, Inc.     

Comparison of lipase-catalysed esterification in supercritical carbon dioxide and in n-hexane

Summary Oleic acid esterification by ethanol has been performed by an immobilized lipase fromMucor miehei in supercritical carbon dioxide and in n-hexane as solvents. In both media, determination of apparent kinetic constants has been achieved and influence of water content has been shown to be different due to various rates of water solubilities. Stability of the lipase has been proved to be correct and similar in both solvents. Inhibition by ethanol excess has been found but is greater in n-hexane. That can explain the higher initial velocities obtained in supercritical carbon dioxide for the highest ethanol concentrations.     

北五味子果实超临界CO2萃取工艺的研究

通过正交设计的试验方法,探讨了超临界CO₂法萃取五味子果实中木脂素的工艺条件,确定了最佳工艺条件为萃取压力30 Mpa,萃取温度50℃,萃取时间120 min。