γ-Irradiation of malic acid in aqueous solutions

The -irradiation of malic acid in aqueous solutions was studied under initially oxygenated and oxygen-free conditions in an attempt to determine the possible interconversion of malic acid into other carboxylic acids, specifically those associated with Krebs cycle. The effect of dose on product formation of the system was investigated. Gas-liquid chromatography combined with mass spectrometry was used as the principal means of identification of the non-volatile products. Thin layer chromotography and direct probe mass spectroscopy were also employed.The findings show that a variety of carboxylic acids are formed, with malonic and succinic acids in greatest abundance. These products have all been identified as being formed in the -irradiation of acetic acid, suggesting a common intermediary. Since these molecules fit into a metabolic cycle, it is strongly suggestive that prebiotic pathways provided the basis for biological systems.     

The γ-irradiation of aqueous acetic acid-clay suspensions

-radiolysis of 0.8 mol dm^–3 aqueous, oxygen-free acetic acid solutions was investigated in the presence or absence of Na-montmorillonite (1–3 g per 10 cm^–3). The systems were irradiated at their natural pH (3.5), and 25 °C in a dose range from 0.01 to 500 kGy. H₂, CH₄, CO, CO₂, and a variety of polycarboxylic acids were formed in all systems. The major features of the radiolysis in the presence of clays were: (1) More solute molecules were decomposed; (2) Carbon dioxide was produced in higher yield; (3) The yield of methane was unaffected; and (4) 44% less polycarboxylic acids were formed. Three possible mechanisms that could account for the observed changes are suggested. The results are important in understanding heterogeneous processes in radiation catalysis and might be significant to prebiotic chemistry.     

α-Chymotrypsin superactivity in aqueous solutions of cationic surfactants

α-Chymotrypsin (α-CT) activity was tested in aqueous media with the following cetyltrialkylammonium bromide surfactants in the series methyl, ethyl, propyl and butyl, different in the head group size, and for the sake of comparison also with the anionic sodium n-dodecyl sulfate and the zwitterionic myristyldimethylammonium propanesulfonate. N-glutaryl-l-phenylalanine p-nitroanilide hydrolysis rate was monitored at surfactant concentration above the critical micellar one. Only some cationic surfactants gave superactivity and the head group size had a major weight. The highest superactivity was measured in the presence of cetyltributylammonium bromide. The effect of both nature and concentration of three different buffers was also investigated. There is a dependence of enzyme superactivity on buffer type. Michaelis–Menten kinetics were found. The binding constants of substrate with micellar aggregates were determined in the used buffers and the effective improvement of reaction rate (at the same free substrate concentration in the medium) was calculated. k_cat significantly increased while K_m was little changed after correction to free substrate concentration. The ratio of k_cat to K_m was between 12 and 35 times higher than in pure buffer, depending on buffer and surfactant concentrations. The increase of α-CT activity (30%) was less important in the presence of 1×10⁻² M tetrabutylammonium bromide, a very hydrophobic salt, unable to micellise. Fluorescence spectra showed differences of enzyme conformation in the presence of various surfactants.     

Physical properties of detergent-based aqueous two–phase systems

The physical behavior of the binary phase systems of the non-ionic polyoxyethylene detergent Agrimul NRE 1205 and water was investigated. This technical detergent can be used for the large-scale recovery of biomolecules in detergent based aqueous two-phase systems. The phase diagram was determined. It shows significant and unexpected differences to highly purified detergents. Very similar to neat detergents the phase diagram can be influenced by auxiliary chemicals thus shifting the entire phase diagram in general to lower temperatures. This was demonstrated by lowering the cloud-point by various additions. The concentration factor, as an important parameter of a first capture step in purification was investigated and modeled. Auxiliary chemicals, temperature change and change in detergent concentration also influence the viscosity and density of the phases. These experimental data are shown. They can help to explain the separation behavior of proteins. In large-scale separations aqueous two-phase systems are separated using disc-stack centrifuges. It is demonstrated that this is not a feasible method for detergent-based aqueous two-phase extraction and the physical reason is presented. This revised version was published online in July 2006 with corrections to the Cover Date.     

High-temperature solvolysis of 2′-deoxyribonucleosides in aqueous amine solutions

Abstract

Degradation of 2′-deoxyribonucleosides in 0.5?M aqueous pyrrolidine at 110?°C proceeds at different rates, ordered as deoxyuridine?>?deoxyadenosine?>?deoxycytidine?>?deoxyguanosine ??deoxythymidine. Deoxyadenosine degradation produces the free base, adenine, while deoxycytidine by deamination produces deoxyuridine, and then uracil. The solvolysis of deoxyadenosine has an activation energy of 23.3?kcal/mol. Ammonolysis is slower than pyrrolidinolysis for deoxyadenosine, but faster for deoxyguanosine. In pyrrolidinolysis of the trinucleotides, d-TGT and d-TAT, the guanine moiety reacts faster than the adenine moiety. These trends are interpreted in terms of the ionization of the guanine moieties under basic conditions, rendering them less susceptible to nucleophilic attack.     

Oxidation of oat β-glucan in aqueous solutions during processing

The study investigated carbonyl group formation along the chain and the chain cleavage of cereal β-glucan during heat treatments, high pressure homogenisation, cold storage and ascorbic acid treatment of aqueous solutions of this soluble dietary fibre. The carbonyl group content and its distribution along the chain were simultaneously determined with the chain cleavage using a HPSEC/labelling method, originally developed for water-insoluble cellulose. Ascorbic acid treatment resulted in a relatively high degree of carbonyl content and extensive degradation of β-glucan, even in concentrations typically found in foods. The thermal oxidation of the β-glucan was considerable at 120 °C in a β-glucan solution with co-extracted compounds from oat ingredient, and in the highly purified solutions in presence of ferrous ions. Oxidation also probably contributed to the molecular properties during high pressure homogenisation, even thou the main degradation mechanism is the hydrolysis caused by mechanical energy. In addition to the cleavage of the β-glucan chain, the formation of compact, high molar mass species or molecule clusters were obtained in the study after ascorbic acid, heat (120 °C) and homogenisation treatments.     

Formation of α-synuclein aggregates in aqueous ethylammonium nitrate solutions

The effect of adding ethylammonium nitrate (EAN), which is an ionic liquid (IL), on the aggregate formation of α-synuclein (α-Syn) in aqueous solution has been investigated. FTIR and Raman spectroscopy were used to investigate changes in the secondary structure of α-Syn and in the states of water molecules and EAN. The results presented here show that the addition of EAN to α-Syn causes the formation of an intermolecular β-sheet structure in the following manner: native disordered state → polyproline II (PPII)-helix → intermolecular β-sheet (α-Syn amyloid-like aggregates: α-SynA). Although cations and anions of EAN play roles in masking the charged side chains and PPII-helix-forming ability involved in the formation of α-SynA, water molecules are not directly related to its formation. We conclude that EAN-induced α-Syn amyloid-like aggregates form at hydrophobic associations in the middle of the molecules after masking the charged side chains at the N- and C-terminals of α-Syn.     

Increased production of β-cyclodextrin using an aqueous two-phase system

Summary -Cyclodextrin(-CD) was produced by cyclodextrin glycosyltransferase(CGTase) in aqueous two-phase system. -CD production from soluble starch was catalyzed by CGTase in dextran-rich bottom phase, and the -CD produced was transferred to PEG-rich top phase in aqueous two-phase system, composed of 7% (w/w) polyethylene glycol(Mr 20,000) and 10% (w/w) dextran(Mr 38,900). Partition coefficients of -CD and CGTase were 1.5 and 0.25, respectively. The total productivity of -CD in aqueous two-phase system was about 3 times of that in dextran phase.     

Recovery of antibiotics by aqueous two-phase partition —Partitioning behavior of pure acetylspiramycin solution in polyethylene glycol/potassium phosphate aqueous two-phase systems

Summary The effects of average molecular weight of PEG, concentrations of PEG and KH₂PO₄ and pH on the partition equilibrium of acetylspiramycin in PEG/KH₂PO₄ aqueous two-phase systems were studied in detail. The partition coefficients of acetylspiramycin in PEG/ KH₂PO₄ systems were measured at room temperature 25 °C. It was found that acetylspiramycin partitioned unevenly in the aqueous two-phase systems composed of PEG and KH₂PO₄ and could be purified by this technique. A suitable phase-forming system (pH=6.7, 12w/w% PEG2000, 11w/w% KH₂PO₄) was found out after partition coefficient (Kp=42) , extraction ratio (=96%) and recovery ratio(R=98.8%) were investigated comprehensively in this paper.Hua qiang is one of the cooperators of the experimetal.     

α-Chymotrypsin-catalyzed synthesis of poly-l-cysteine in a frozen aqueous solution

Poly-l-cysteine (PLCys) is drawing attention as a potential sorbent of thiol (SH)-reactive toxic heavy metal ions in the wastewater and polluted soils. However, preparation of PLCys relies on chemically synthesized polymers, in which SH groups must be protected and deprotected prior to use. On the other hand, α-chymotrypsin polymerized l-cysteine ethyl ester in a frozen aqueous solution, provides PLCys with degree of polymerization from 6 to 11 without blocking of SH groups. Kinetic analyses suggested that the acylation of α-chymotrypsin with the initial substrate was a rate-limiting step in the enzymatic polymerization. The peptide yields reached 85% and 65% of SH groups in PLCys were assumed to be free forms. Although detail information on correlation between the state of SH groups and heavy metal adsorption properties of PLCys should be explored in further studies, the present study for the first time proposed an easy method for synthesis of PLCys requiring neither SH-protection nor -deprotection.     

α-Amylase production in aqueous two-phase systems with Bacillus amyloliquefaciens

-Amylase production was studied in Bacillus amyloliquefaciens in aqueous two-phase systems composed of polyethyleneglycol (PEG)/dextran T500. Cells and enzyme were obtained in different phases when phase systems were applied to the growth media. Effects of different molecular weights and concentrations of polymers on differences of enzyme separation were established. The effect of PEG used in the system to the release of enzyme was investigated.     

α-amylase production in aqueous two-phase systems with Bacillus subtilis

The production of α-amylase (1,4-α-d-glucan glucanohydrolase, EC 3.2.1.1) by Bacillus subtilis has been studied in repeated batch fermentations in aqueous two-phase systems. In a phase system composed of PEG 600, 8% (w/w), PEG 3350, 5% (w/w)/Dextran T 500, 2% (w/w), 82% of the enzyme partitioned to the top phase. The enzyme concentration in the top phase reached 0.85–1.35 U ml^?1 during the fermentations compared with 0.58 U ml^?1 in the reference fermentation. In the phase system composed of PEG 3350, 9% (w/w)/Dextran T 500, 2% (w/w), 73% of the enzyme partitioned to the top phase. However, the enzyme concentration in this phase system reached only 0.35 U ml^?1 in the top phase. The bacterial cells were microscopically observed to partition totally to the bottom phase in the aqueous two-phase system used. The results are discussed in relation to recirculation of cells by immobilizing to a solid matrix. Extraction of the product to the top phase and the effect of the phase polymers, especially PEG, on the production are also discussed.     

The effects of γ-rays on poly-L-glutamic acid in aqueous solution

Summary Salt-free and 0.2 M NaCl oxygenated aqueous solutions of poly-L-glutamic acid were irradiated with⁶⁰Co--radiation at variouspH's to examine whether or not the changes caused by the exposure to ionizing radiation depend onpH, that is, the conformations of polypeptide.TheG-values (the number of main-chain scissions per 100 eV of energy absorbed) in both salt-free and 0.2 M NaCl solutions of poly-L-glutamic acid were found to change sharply withpH. and to have a maximum value at thepH of a mid-point of helix-coil transition. The change ofG-values withpH was discussed in terms of the conformational change of poly-L-glutamic acid.     

Phase diagrams for dextran-PEG aqueous two-phase systems at 22°C

Summary We have determined phase diagrams at 22°C for the aqueous two-phase systems composed of dextran, polyethylene glycol, and water. The effects of polyethylene glycol and dextran molecular weight on phase separation are reported. These phase diagrams provide more complete data for dextran/PEG/water system, and will be needed for the correlation of biomolecule partitioning.     

Separation of recombinant β-glucuronidase from transgenic tobacco by aqueous two-phase extraction

Transgenic plants hold many promises as viable production hosts for therapeutic recombinant proteins. Many efforts have been devoted to increase the expression level of the proteins, but the efforts for developing economic processes to purify those proteins are lacking. In this report, aqueous two-phase extraction (ATPE) was investigated as an alternative for the separation of an acidic recombinant protein, β-glucuronidase (rGUS), from transgenic tobacco. Screening experiments by fractional factorial designs showed that PEG concentration and ionic strength of the system significantly affected the partitioning of native tobacco proteins and GUS. Response surface methodology was used to determine an optimized aqueous two-phase system for the purification of rGUS from transgenic tobacco. In a 13.4% (w/w) PEG 3400/18% (w/w) potassium phosphate system, 74% of the rGUS was recovered in the top PEG-rich phase while more than 90% of the native tobacco proteins were removed in the interphase and the bottom phase. A purification factor of about 20 was achieved in this process. The most important impurity from tobacco, Rubisco, was largely removed from the rGUS in the recovered phase.     

Physical characterisations of a single-stage Kühni-type aqueous two-phase extraction column

The main parameters which influence the behaviour of phase separation in a single-stage Kühni-type aqueous two-phase extraction column containing polyethylene (PEG) and di-potassium hydrogen phosphate were characterised. Two aqueous two-phase system (ATPS) composed of 12% (w/w) PEG 1450 and 12% (w/w) di-potassium hydrogen phosphate (designated as 12/12) and 12% (w/w) PEG 1450 and 11% (w/w) di-potassium hydrogen phosphate (designated as 12/11) were chosen in this study. The hold-up ɛ_D increased with increasing impeller speeds and mobile phase flow rates. Phase separation for the 12/11 system was slower than that for the 12/12 system, which resulted in higher dispersed phase hold-up values for the 12/11 system. For 12/12 system, mass transfer of plasmid DNA (pDNA) from the dispersed mobile phase to the stationary phase increased rapidly with increasing impeller speeds of 130, 160 and 200 rpm which was reflected in the decreased values for C_T/C_To. The degree of back-mixing quantified by the axial dispersion coefficient D_ax was estimated to be 2.7 × 10⁻⁶ m² s⁻¹.     

Production of β-glucosidase withAspergillus phoenicis QM329 in aqueous two-phase systems

Summary The production of -glucosidase withAspergillus phoenicis QM 329 was studied in two different aqueous two-phase systems: polyethylene glycol (PEG) 1550 7.5%/Dextran T2000 9.5% and PEG 8000 4%/polyvinyl alcohol (PVA) 14000 8%. The enzyme concentrations in the top phase of the phase systems were 3.4 IU/ml and 3.2 IU/ml, respectively, compared with 2.0 IU/ml obtained in a regular medium. The total amount of -glucosidase obtained in the phase systems was 265 IU and 176 IU, respectively, compared with 200 IU in a regular medium.     

A whole-cell process for the production of ε-caprolactone in aqueous media

ε-Caprolactone is an industrially important intermediate produced in multi-10,000 ton scale annually with broad applications. We report on a whole-cell biocatalytic conversion of cyclohexanol to ε-caprolactone using the combination of alcohol dehydrogenase (ADH) with two stability-improved variants (QM and M15) of the Baeyer-Villiger monooxygenase CHMO with a special focus on process development at the 200 mM scale. Influence of parameters such as volumetric mass transfer co-efficient, stirrer speed and catalytic loading (amount of E. coli whole-cells expressing ADH and CHMO) on the process efficiency were studied and optimised. This resulted in over 98% conversion, a product titer of 20 g L^–1 and an isolated product amount of 9.1 g (80%). This corresponds to a space-time yield of 1.1 g L^–1 h⁻¹ and a reaction yield (mole of product per mole substrate) of 0.9. Comparing the two CHMO variants a significant difference in catalytic yield (weight of product to weight of catalyst; 0.6 vs 0.3) was observed without any inherent changes in the process. Hence, the reported process can accommodate in the future improved variants of the CHMO.     

Excess enthalpies of aqueous solutions of mono- and oligo-saccharide at 25°

The heats of dilution in water of d-xylose, d-fructose, d-galactose, d-mannose, lactose, and raffinose have been determined calorimetrically at 25°. The calorimetric data, expressed in terms of excess enthalpy, lead to an evaluation of pair- and triplet-interaction coefficients. Osmotic data, where known, permit the analogous coefficients of the excess free energy to be obtained and thence those of the excess entropy. Analysis of the excess functions and comparison with spectroscopic properties permits some qualitative hypotheses to be formulated on the molecular interactions occurring in these solutions.     

LPS–protein aggregation influences protein partitioning in aqueous two-phase micellar systems

Lipopolysaccharide endotoxins (LPS) are the most common pyrogenic substances in recombinant peptides and proteins purified from Gram-negative bacteria, such as Escherichia coli. In this respect, aqueous two-phase micellar systems (ATPMS) have already proven to be a good strategy to purify recombinant proteins of pharmaceutical interest and remove high LPS concentrations. In this paper, we review our recent experimental work in protein partitioning in Triton X-114 ATPMS altogether with some new results and show that LPS–protein aggregation can influence both protein and LPS partitioning. Green fluorescent protein (GFPuv) was employed as a model protein. The ATPMS technology proved to be effective for high loads of LPS removal into the micelle-rich phase (%REM_LPS?>?98 %) while GFPuv partitioned preferentially to the micelle-poor phase (K _GFPuv?<?1.00) due to the excluded-volume interactions. However, theoretically predicted protein partition coefficient values were compared with experimentally obtained ones, and good agreement was found only in the absence of LPS. Dynamic light scattering measurements showed that protein–LPS interactions were taking place and influenced the partitioning process. We believe that this phenomenon should be considered in LPS removal employing any kind of aqueous two-phase system. Nonetheless, ATPMS can still be considered as an efficient strategy for high loads of LPS removal, but being aware that the excluded-volume partitioning theory available might overestimate partition coefficient values due to the presence of protein–LPS aggregation.