Removal of toxic preservatives in pharmaceutical preparations of insulin by the use of ultra-stable zeolite Y

Ultra-stable zeolite Y and mordenite with pore sizes of 0.75 and 0.70 nm, respectively, showed the capacity to bind phenol and m-cresol rapidly. Phenol and m-cresol are used as preservatives in pharmaceutical preparations for humans and, with the use of a 15 mg filter of ultra-stable zeolite Y, 98 % of the preservative in a 200 l pharmaceutical insulin preparation, Actrapid®, was removed after 5 s of passage through the filter. The insulin content in the filtrate was not disminished. © Rapid Science Ltd. 1998     

The use of zeolites as slow release anthelmintic carriers

This work examines the ability of commercial zeolite Y to act as a slow release agent for a number of anthelmintic drugs. Administration to rats, dosed with Nippostrongylus brasiliensis, of pyrantel and/or fenbendazole and pigs, dosed with Ascaris and Oesophagostomum, of dichlorvos (DDVP) loaded onto zeolite Y was more successful in killing adult worms than administration of the pure drug alone. The zeolite Y was used as supplied for initial studies and then later dealuminated for further studies. The drug loadings were monitored by thermal analysis and the loaded zeolites were used in several field trials. The results indicate that zeolite Y is a suitable vehicle for the slow release of some anthelmintics. The slow release of drug from the zeolite matrix improved its efficacy.     

Adsorption of Adenine and Thymine on Zeolites: FT-IR and EPR Spectroscopy and X-Ray Diffractometry and SEM Studies

The interactions of adenine and thymine with and adsorption on zeolites were studied using different techniques. There were two main findings. First, as shown by X-ray diffractometry, thymine increased the decomposition of the zeolites (Y, ZSM-5) while adenine prevented it. Second, zeolite Y adsorbed almost the same amount of adenine and thymine, thus both nucleic acid bases could be protected from hydrolysis and UV radiation and could be available for molecular evolution. The X-ray diffractometry and SEM showed that artificial seawater almost dissolved zeolite A. The adsorption of adenine on ZSM-5 zeolite was higher than that of thymine (Student-Newman-Keuls test-SNK p<0.05). Adenine was also more greatly adsorbed on ZSM-5 zeolite, when compared to other zeolites (SNK p<0.05). However the adsorption of thymine on different zeolites was not statistically different (SNK p>0.05). The adsorption of adenine and thymine on zeolites did not depend on pore size or Si/Al ratio and it was not explained only by electrostatic forces; rather van der Waals interactions should also be considered.     

Effective Inhibition of Ammonium Released from Heavily Contaminated Sediments through Selective Oxidation with Zeolite Layer

Abstract

In order to study the remediation effect of heavily contaminated sediments, the experiments to repair heavily contaminated sediments were carried out under selective and nonselective oxidation conditions. Results showed that a lot of denitrifying bacteria was detected on the surface of modified zeolite by fluorescence in situ hybridization (FISH) after inoculating both nitrifying and denitrifying bacteria for 7?days. Up to 3.69?mg/g, in-situ regeneration of ammonium on zeolite loading with high ammonium (ammonium adsorption: 4.20?m/g) was obtained, which was 1.42 times that of nonselective oxidation (2.60?mg/g). This indicated that the in-situ regeneration rate of zeolite under high ammonium adsorption (5.0?mg/g) and high bacterial inoculum (80?mL/g) was enhanced. Moreover, only 1.50?mg/L total nitrogen with 84% inhibition in the overlying water under selective oxidation conditions was observed, which was 2.37 times the inhibition percentage of modified zeolite under nonselective oxidation conditions. The results illuminated that effective inhibition of ammonium released from heavily contaminated sediments can be achieved through selective oxidation with zeolite layer. At the same time, the in-situ service life of attached biofilm-modified zeolite under selective oxidation conditions was 5.87?years, which was extended by 3?years compared with nonselective oxidation conditions.     

Liquid growth hormone: preservatives and buffers

Growth hormone (GH) treatment is a successful medical therapy for children and adults with GH deficiency as well as for growth retardation due to chronic renal disease, Turner syndrome and in children born small for gestational age. For all of these conditions, treatment is long term and patients receive daily subcutaneous injections of GH for many years. Patient compliance is therefore of critical importance to ensure treatment benefit. One of the major factors influencing compliance is injection pain. Besides the injection device used, pain perception and local tissue reaction following injection are dependent on the preservative used in the formulation and the concentration of GH. Injection pain may also be related to the buffer substance and injection volume. A liquid formulation of GH, Norditropi SimpleXx, has been developed that dispenses with the need for reconstitution before administration. The formulation uses phenol (3 mg/ml) as a preservative (to protect product from microbial degradation or contamination) and histidine as a buffer. Alternative preservatives used in other GH formulations include m-cresol (9 mg/ml) and benzyl alcohol (3-9 mg/ml). Buffering agents include citrate and phosphate. Phenol has been successfully used as a preservative in drug formulations for more than 50 years and is considered a safe and effective agent which complies with strict international requirements for preservatives in drug formulations. In toxicological studies, no or only mild local reactions have been observed following subcutaneous administration of phenol (7.5 mg/ml), m-cresol (3-4 mg/ml) and benzyl alcohol (9 mg/ml). No general toxicity reactions were observed after subcutaneous administration of these agents. Clinical evaluation of the preservatives and buffers used in Norditropin SimpleXx showed that pain perception was similar between formulations containing phenol and benzyl alcohol, whereas m-cresol was associated with more painful injections than benzyl alcohol. Furthermore, patients reported more pain following injection of a citrate-buffered solution than after a histidine-buffered solution. More pain was also reported following large volume injections and following injections with solutions containing high protein concentrations. In summary, optimization of the preservative and buffer content of a liquid GH formulation may reduce injection pain and lead to improved patient compliance.     

Culture methods for obtaining m-cresol-degrading methanogenic consortia

Studies of the metabolism of m-cresol under methanogenic conditions have been hampered by difficulties in enriching and maintaining active consortia. With anaerobic sewage sludge as an inoculum, m-cresol degradation was shown to be inhibited by sodium sulfide at concentrations typically used to pre-reduce culture medium. In enrichment cultures, the acclimation time for m-cresol degradation was shortened from 61 days to 37 days by using diluted (24% vol/vol) sludge rather than concentrated (96%) sludge, which contained 0.8 mM total sulfide. The m-cresol degrading activity of enrichment cultures transferred to fresh medium was greater when iron nails or amorphous ferrous sulfide were used as a reducing agent in place of sodium sulfide.     

Effect of Dicranopteris dichotoma on spectroscopic characteristic of dissolved organic matter in red soil erosion area

Aims Dissolved organic matter (DOM) is the most active component of organic matters in soils, and plays an important role in carbon cycles. It is a mixed organic compound with varying molecular sizes and weights. We aimed to explore the impacts of Dicranopteris dichotoma coverage on quantity and structure of DOM after vegetation restoration in severely eroded red soil region. Methods A typical sequence of vegetation restoration (Y0, without ecological restoration; Y13, ecological restoration for 13 years; Y31, ecological restoration for 31 years) was selected as the research object in Hetian Town, Changting County, Fujian Province, China. At each experimental site, soils were subject to three treatments—NRd, not removed D. dichotoma; Rd, removed D. dichotoma; and CK, control, and the effects of D. dichotoma on the spectral characteristics of DOM were evaluated.Important findings The results indicated that the quantity of soil DOC under NRd treatment of the Y0, Y13 and Y31 was 7.61, 4.83, and 5.47 times higher than their CK treatment, respectively. The Rd treatment had significantly lower DOC than that under NRd treatments, and it was 1.84, 4.12, and 4.73 times higher than their CK treatments, respectively. Thus the D. dichotoma had exerted significant effects on the quantity of soil DOM. The Aromaticity index (AI), emission fluorescence spectrum humification index (HIX_em) and synchronous fluorescence spectrum humification index (HIX_syn) of DOM under the NRd treatment were significantly higher than those of the CK treatments in Y13 and Y31, respectively. However, the ratio of ultraviolet-visible light absorption photometric quantity at 250 nm wavelength to ultraviolet-visible light absorption photometric quantity at 365 nm wavelength (E₂:E₃) had an opposite trend. It showed that the DOM structure in soils covered by D. dichotoma contained more aromatic nucleus and had higher aromaticity and humification, and DOM molecular was larger. In addition, the AI and humification index (HIX) of DOM under the Rd treatment was significantly decreased compared with the NRd treatment. Similar results were observed by analysis of emission and synchronous fluorescence spectrum, and by the Fourier infrared transmission spectrum analysis. These results suggest that D. dichotoma had positive impacts on the complexity of DOM structure, but it was a long and slow process. The DOM spectral analysis showed that the soil DOM covered by D. dichotoma had a stable and complex structure and was easily adsorbed by soil colloid. As a result, Dicranopteris dichotoma had a positive effect on the accumulation of soil organic carbon.     

Anaerobic degradation of m-cresol in anoxic aquifer slurries: carboxylation reactions in a sulfate-reducing bacterial enrichment.

The anaerobic biodegradation of m-cresol was observed in anoxic aquifer slurries kept under both sulfate-reducing and nitrate-reducing but not methanogenic conditions. More than 85% of the parent substrate (300 microM) was consumed in less than 6 days in slurries kept under the former two conditions. No appreciable loss of the compound from the corresponding autoclaved controls was measurable. A bacterial consortium was enriched from the slurries for its ability to metabolize m-cresol under sulfate-reducing conditions. Metabolism in this enrichment culture was inhibited in the presence of oxygen or molybdate (500 microM) and in the absence of sulfate but was unaffected by bromoethanesulfonic acid. The consortium consumed 3.63 mol of sulfate per mol of m-cresol degraded. This stoichiometry is about 87% of that theoretically expected and suggests that m-cresol was largely mineralized. Resting-cell experiments demonstrated that the degradation of m-cresol proceeded only in the presence of bicarbonate. 4-Hydroxy-2-methylbenzoic acid and acetate were detected as transient intermediates. Thus, the parent substrate was initially carboxylated as the primary degradative event. The sulfate-reducing consortium could also decarboxylate p- but not m-hydroxybenzoate to near stoichiometric amounts of phenol, but this reaction was not sulfate dependent. The presence of p-hydroxybenzoate in the medium temporarily inhibited m-cresol metabolism such that the former compound was metabolized prior to the latter and phenol was degraded in a sequential manner. These findings help clarify the fate of a common groundwater contaminant under sulfate-reducing conditions.     

Anaerobic degradation of m-cresol in anoxic aquifer slurries: carboxylation reactions in a sulfate-reducing bacterial enrichment

The anaerobic biodegradation of m-cresol was observed in anoxic aquifer slurries kept under both sulfate-reducing and nitrate-reducing but not methanogenic conditions. More than 85% of the parent substrate (300 microM) was consumed in less than 6 days in slurries kept under the former two conditions. No appreciable loss of the compound from the corresponding autoclaved controls was measurable. A bacterial consortium was enriched from the slurries for its ability to metabolize m-cresol under sulfate-reducing conditions. Metabolism in this enrichment culture was inhibited in the presence of oxygen or molybdate (500 microM) and in the absence of sulfate but was unaffected by bromoethanesulfonic acid. The consortium consumed 3.63 mol of sulfate per mol of m-cresol degraded. This stoichiometry is about 87% of that theoretically expected and suggests that m-cresol was largely mineralized. Resting-cell experiments demonstrated that the degradation of m-cresol proceeded only in the presence of bicarbonate. 4-Hydroxy-2-methylbenzoic acid and acetate were detected as transient intermediates. Thus, the parent substrate was initially carboxylated as the primary degradative event. The sulfate-reducing consortium could also decarboxylate p- but not m-hydroxybenzoate to near stoichiometric amounts of phenol, but this reaction was not sulfate dependent. The presence of p-hydroxybenzoate in the medium temporarily inhibited m-cresol metabolism such that the former compound was metabolized prior to the latter and phenol was degraded in a sequential manner. These findings help clarify the fate of a common groundwater contaminant under sulfate-reducing conditions.     

High‐throughput protein refolding screening method using zeolite

We established a 96‐well‐plate‐based refolding screening system using zeolite. In this system, protein denatured and solubilized with 6 M guanidine hydrochloride is adsorbed onto zeolite placed in a 96‐well plate. The refolding conditions can be tested by incubating the samples with refolding buffers under various conditions of pH, salts, and additives. In this study, we chose green fluorescent protein as the model protein. Green fluorescent protein was expressed as inclusion bodies, and we tested the effects of four pH conditions and six additives on its refolding. The results demonstrate that green fluorescent protein was more efficiently refolded with zeolite than with the conventional dilution method. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

新型固定化硝化细菌和好氧反硝化细菌处理氨氮废水

以改性沸石、聚乙烯醇、海藻酸钠作为固定化载体材料,硼酸和氯化钙作为交联剂,采用吸附-包埋-交联法将硝化细菌和好氧反硝化细菌复合固定化制备成微生物小球.通过复合菌配比实验,考察其对氨氮的去除率以及亚硝酸盐和硝酸盐的累积量;对制成的固定化小球做四因素三水平的正交实验,考察不同条件下对氨氮的去除率.结果表明,硝化细菌和好氧反硝化细菌配比为3:2时,氨氮去除率最高达82.32%,亚硝酸盐和硝酸盐的累积量为0.032mg·L^-1和0.053 mg·L^-1;通过正交实验,确定沸石投加量为2g·100mL^-1、温度为30℃、pH值为7.5、振荡速度为130r·min^-1时,对氨氮达到最好的去除效果,去除率达90.31%,此法制得的小球机械性能和吸水性能良好.     

Utilization of zeolite Y in the removal of anionic,cationic and nonionic detergents during purification of proteins

Summary Hydrophobie zeolite Y was used to adsorb detergents from protein solutions and within one minute the commonly used detergents sodium dodecyl sulfate, cetyl trimethyl ammonium bromide, and Triton X-100 at concentrations of 10 mg/ml were adsorbed to a level below their critical micelle concentrations. From the detergent depleted solutions 77 to 85 % of the proteins were recovered; the lower value was obtained with protein concentration below one mg/ml.     

Biocatalyst engineering exerts a dramatic effect on selectivity of hydrolysis catalyzed by immobilized lipases in aqueous medium

It has been found that enantioselectivity of lipases is strongly modified when their immobilization is performed by involving different areas of the enzyme surface, by promoting a different degree of multipoint covalent immobilization or by creating different environments surrounding different enzyme areas. Moreover, selectivity of some immobilized enzyme molecules was much more modulated by the experimental conditions than other derivatives. Thus, some immobilized derivatives of Candida rugosa (CRL) and C. antarctica-B (CABL) lipases are hardly enantioselective in the hydrolysis of chiral esters of (R,S)-mandelic acid under standard conditions (pH 7.0 and 25°C) (E<2). However, other derivatives of the same enzymes exhibited a very good enantioselectivity under nonstandard conditions. For example, CRL adsorbed on PEI-coated supports showed a very high enantio-preference towards S-isomer (E=200) at pH 5. On the other hand, CABL adsorbed on octyl-agarose showed an interesting enantio-preference towards the R-isomer (E=25) at pH 5 and 4°C. These biotransformations are catalyzed by isolated lipase molecules acting on fully soluble substrates and in the absence of interfacial activation against external hydrophobic interfaces. Under these conditions, lipase catalysis may be associated to important conformational changes that can be strongly modulated via biocatalyst and biotransformation engineering. In this way, selective biotransformations catalyzed by immobilized lipases in macro-aqueous systems can be easily modulated by designing different immobilized derivatives and reaction conditions.     

Anaerobic Degradation of m-Cresol by a Sulfate-Reducing Bacterium

m-Cresol metabolism under sulfate-reducing conditions was studied with a pure culture of Desulfotomaculum sp. strain Groll. Previous studies with a sulfate-reducing consortium indicated that m-cresol was degraded via an initial para-carboxylation reaction. However, 4-hydroxy-2-methylbenzoic acid was not degraded by strain Groll, and no evidence for ring carboxylation of m-cresol was found. Strain Groll readily metabolized the putative metabolites of a methyl group oxidation pathway, including 3-hydroxybenzyl alcohol, 3-hydroxybenzaldehyde, 3-hydroxybenzoic acid, and benzoic acid. Degradation of these compounds preceded and inhibited m-cresol decay. 3-Hydroxybenzoic acid was detected in cultures that received either m-cresol or 3-hydroxybenzyl alcohol, and trace amounts of benzoic acid were detected in m-cresol-degrading cultures. Therefore, we propose that strain Groll metabolizes m-cresol by a methyl group oxidation pathway which is an alternate route for the catabolism of this compound under sulfate-reducing conditions.     

Effect of natural zeolite (clinoptilolite) on microbial decomposition processes in stored pig-slurry solids

The solid fraction (SF) of pig slurry obtained in the first stage of aerobic slurry treatment was amended with 1 and 2 % zeolite (clinoptilolite) and stored for 12 weeks under anaerobic conditions or with turning after 3 and 6 weeks of storage. In addition to that SF was mixed with 2 % zeolite, 50 % (V/V) sawdust, and both sawdust and zeolite, and stored for 6 weeks with turning after 1 and 3 weeks. Plate counts of psychrophilic, mesophilic, coliform and fecal coliform bacteria, determined during the storage, corresponded to the development of temperature, in the core of the substrates. An effect of amendment of SF with zeolite and sawdust on plate counts of selected bacteria was observed, dependent on the zeolite dose. The thermophilic phase was not reached in any of the investigated substrates. The populations of fecal coliforms in the substrate amended with 1 % zeolite and turned after 3 and 6 weeks decreased after 11 weeks down to 500 CFU/g substrate. Presented at theInternational Conference on Recent Problems in Microbiology and Immunology, Košice (Slovakia), 13–15 October 1999.     

Modulation of Mucor miehei lipase properties via directed immobilization on different hetero-functional epoxy resins: Hydrolytic resolution of (R,S)-2-butyroyl-2-phenylacetic acid

Purified lipase from Mucor miehei (MML) has been covalently immobilized on different epoxy resins (standard hydrophobic epoxy resins, epoxy-ethylenediamine, epoxy-iminodiacetic acid, epoxy-copper chelates) and adsorbed via interfacial activation on octadecyl-Sepabeads support (fully coated with very hydrophobic octadecyl groups). These immobilized enzyme preparations were used under slightly different conditions (temperature ranging from 4 to 25 °C and pH values from 5 to 7) in the hydrolytic resolution of (R,S)-2-butyroyl-2-phenylacetic acid.

Different catalytic properties (activity, specificity, enantioselectivity) were found depending on the particular support used. For example, the epoxy-iminodiacetic acid-Sepabeads gave the most active preparation at pH 7 while, at pH 5, the ethylenediamine-Sepabeads was superior.

More interestingly, the enantiomeric ratio (E) also depends strongly on the immobilized preparation and the conditions employed. Thus, the octadecyl-MML preparation was the only immobilized enzyme derivative which exhibited enantioselectivity towards R isomer (with E values ranging from 5 at 4 °C and pH 7 to 1.2 at pH 5 and 25 °C).

The other immobilized preparations, in contrast, were S selective. Immobilization on iminodiacetic acid-Sepabeads afforded the catalyst with the highest enantioselectivity (E=59 under optimum conditions).     

Dot assay for determining adhesive interactions between yeasts and bacteria under controlled hydrodynamic conditions

Candida belongs to the normal human microflora and are found adhering to a number of human body tissues as well as to a variety of biomaterials implants. Often, yeasts adhere in association with bacteria, but to date there is no definitive assay to investigate adhesive interactions between yeasts and bacteria adhering on surfaces. Although we recently described the use of a parallel plate flow chamber to this purpose [Millsap, K.W., Bos, R., Van der Mei, H.C., Busscher, H.J., 1998. Adhesive interactions between medically important yeasts and bacteria. FEMS Microbiol. Rev. 21, 321–336], the method was slow and evaluation of a large number of strains showed major biological variation between experiments. Here, we describe a new assay for the simultaneous determination of the adhesive interactions between yeasts and different bacterial strains on a surface under controlled hydrodynamic conditions. On an acrylic surface, the presence of adhering bacteria suppressed adhesion of Candida albicans ATCC 10261 to various degrees, depending on the bacterial strain involved. Suppression of C. albicans ATCC 10261 adhesion was strongest by Actinomyces naeslundii T14V-J1, while adhering Streptococcus gordonii NCTC 7869 caused the weakest suppression of yeast adhesion. When adhering yeasts and bacteria were challenged with the high detachment force of a passing liquid–air interface, the majority of the yeasts detached, while C. albicans adhering on the control, bare polymethylmethacrylate surface formed aggregates. Summarizing, this study presents a new method to determine suggested adhesive interactions between yeasts and adhering bacteria under controlled hydrodynamic conditions. However, the results seem to indicate that these adhesive interactions may well not exist, but that instead different bacterial strains have varying abilities to discourage yeast adhesion.     

Variables that affect xylitol production from sugarcane bagasse hydrolysate in a zeolite fluidized bed reactor

The operational conditions for xylitol production by fermentation of sugarcane bagasse hydrolysate in a fluidized bed reactor with cells immobilized on zeolite were evaluated. Fermentations were carried out under different conditions of air flowrate (0.0125-0.0375 vvm), zeolite mass (100-200 g), initial pH (4-6), and xylose concentration (40-60 g/L), according to a 2(4) full factorial design. The air flowrate increase resulted in a metabolic deviation from product to biomass formation. On the other hand, the pH increase favored both the xylitol yield (Y(P/S)) and volumetric productivity (Q(P)), and the xylose concentration increase positively influenced the xylitol concentration. The best operational conditions evaluated were based on the use of an air flowrate of 0.0125 vvm, 100 g of zeolite, pH 6, and xylose concentration of 60 g/L. Under these conditions, 38.5 g/L of xylitol were obtained, with a Y(P/S) of 0.72 g/g, Q(P) of 0.32 g/L.h, and cell retention of 25.9%.     

Kinetic quantitation of sulfur-oxidizing bacteria adsorbed on sulfur

A hyperbolic equation was fitted to the time dependence of Thiobacillus ferrooxidans adsorption on sulfur. This procedure allowed the determination of an asymptote value which represented a free cell count at equilibrium. The data thus obtained were used to calculate the numbers of adsorbed bacteria without attainment of equilibrium. The maximum number of adsorbed bacteria based on the Langmuir isotherm was 8.3 × 10⁹ per g of sulfur.     

Application of Freundlich and Langmuir models to multistage purification process to remove heavy metal ions by using Schizomeris leibleinii

The adsorption of iron(III), lead(II) and cadmium(II) ions onto Schizomeris leibleinii, a green alga, was studied with respect to initial pH, temperature, initial metal ion and biomass concentration to determine the optimum adsorption conditions. Optimum initial pH for iron(III), lead(II) and cadmium(II) ions were 2.5, 4.5 and 5.0 at optimum temperature 30°C, respectively. The initial adsorption rates increased with increasing initial iron(III), lead(II) and cadmium(II) ion concentrations up to 100, 100 and 150 mg l⁻¹, respectively. The Freundlich and Langmuir adsorption isotherms were developed at various initial pH and temperature values. The adsorption of these metal ions to S. leibleinii was investigated in a two-stage mixed batch reactor. The residual metal ion concentrations (C_eq) at equilibrium at each stage for a given ‘quantity of dried algae (X₀)/volume of solution containing heavy metal ion (V₀)’ ratio were calculated using Freundlich and Langmuir isotherm constants. The experimental biosorption equilibrium data for iron(III), lead(II) and cadmium(II) ions were in good agreement with those calculated by both Freundlich and Langmuir models. The adsorbed iron(III), lead(II) and cadmium(II) ion concentrations increased with increasing X₀/V₀ ratios while the adsorbed metal quantities per unit mass of dried algae decreased.