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Strategy for selection of methods for separation of bioparticles from particle mixtures.

The desired product of bioprocesses is often produced in particulate form, either as an inclusion body (IB) or as a crystal. Particle harvesting is then a crucial and attractive form of product recovery. Because the liquid phase often contains other bioparticles, such as cell debris, whole cells, particulate biocatalysts or particulate by-products, the recovery of product particles is a complex process. In most cases, the particulate product is purified using selective solubilization or extraction. However, if selective particle recovery is possible, the already high purity of the particles makes this downstream process more favorable. This work gives an overview of typical bioparticle mixtures that are encountered in industrial biotechnology and the various driving forces that may be used for particle-particle separation, such as the centrifugal force, the magnetic force, the electric force, and forces related to interfaces. By coupling these driving forces to the resisting forces, the limitations of using these driving forces with respect to particle size are calculated. It shows that centrifugation is not a general solution for particle-particle separation in biotechnology because the particle sizes of product and contaminating particles are often very small, thus, causing their settling velocities to be too low for efficient separation by centrifugation. Examples of such separation problems are the recovery of IBs or virus-like particles (VLPs) from (microbial) cell debris. In these cases, separation processes that use electrical forces or fluid-fluid interfaces show to have a large potential for particle-particle separation. These methods are not yet commonly applied for large-scale particle-particle separation in biotechnology and more research is required on the separation techniques and on particle characterization to facilitate successful application of these methods in industry.

Biological Products↗

[Interaction between microorganisms and heavy metals and its application].

Interactions between microorganisms and heavy metals were expatriated in many ways. Because of their resistance and detoxification to heavy metals, microorganisms are able to leach, absorb and transform heavy metals, which has been actively applied to extract heavy metals from low-rate ore in mine exploitation. Although heavy metals are toxic to microorganisms population and harmful to its processes, some special microorganisms have been applied to the treatment of industrial waste materials and the remediation of soils polluted by heavy metals. The application of microbiological biomass and activity to evaluating the pollution situation and ecological risk of heavy metals in environment media is also significant.

Bacteria↗

Effects of chemical, physical, and technological processes on the nature of food allergens.

A review is presented of studies of different processing techniques and their effect on the allergenicity and antigenicity of certain allergenic foods. An overview of investigated technologies is given with regard to their impact on the protein structure and their potential application in the production of hypoallergenic foods. The use of physical processes (such as heating, high pressure, microparticulation, ultrafiltration, and irradiation), chemical processes (such as proteolysis, fermentation, and refining by extraction), and biotechnological approaches, as well as the effects of these processes on individual allergenic foods, are included. Additionally, the implications of food processing for food allergen analysis with respect to food safety assessment and industrial quality control are briefly discussed.

Allergens↗

Lead removal and recovery from battery industry wastewaters by soluble starch xanthate.

Treatment, removal and recovery of lead (3 mg/L) from battery industry wastewaters have been investigated utilising a chemical precipitation process with soluble starch xanthate (SX) at pH 5-6. A reactant ratio, i.e., SX/Pb(II) = 6 mol/mol, a reaction time of 15 min., the addition of 15 mg/L of a cationic polyelectrolyte and a final filtration gave residual lead concentrations in the liquid phase less than 0.2 mg/L, well below the maximum limit established by the EU Directive. Lead was extracted from the obtained sludge by oxidation with sodium hypochlorite or hydrogen peroxide solutions. The amounts of oxidant needed were quantified as 13.5 mol NaClO/mol Pb and one order of magnitude larger, for H2O2, the latter due to the competitive disproportion reaction of the oxidant. The metal extraction was quantitative using sodium hypochlorite; when hydrogen peroxide was used, the formation of insoluble PbSO4 (Anglesite) gave a 80% metal extraction. In both cases molar ratios between sulphate and lead ions in the extracted solutions were in the range 2.1-2.2, in agreement with the stoichiometries of the reactions. Lead can be quantitatively recovered from the extracted (NaClO) solutions, for reuse, after a chemical precipitation process with 1M NaOH at pH 9-9.5, in the form of hydrocerussite [Pb3(CO3)2(OH)2].

Chemical Precipitation↗

Safety evaluation of a natural tomato oleoresin extract derived from food-processing tomatoes.

Experimental and epidemiological studies indicate that consumption of tomato products containing high amounts of lycopene is associated with lowered cancer risk. The protective effects of lycopene may be related to its antioxidant potential. Lycopene has been demonstrated to inhibit oxidation. A proprietary, natural tomato oleoresin extract (NTOE), is a purified tomato oleoresin containing 6% lycopene produced from tomatoes. NTOE was evaluated for toxicological effects, and found the 50% lethal dose (LD(50)), derived from the acute oral toxicity study, was greater than 5000 mg/kg body weight. The no-observed-adverse-effect level (NOAEL) derived from the 13-week study was 4500 mg/kg/day. Acute dermal toxicity study of NTOE found no toxicity at 2000 mg/kg body weight. NTOE lacked dermal irritation in the rabbit model, but was found to have moderate eye-irritant capabilities. NTOE tested at 5% (w/w) in petroleum jelly was a moderate sensitizer in the guinea pig model. There was no evidence of mutagenic potential up to 5000 microg/plate, as determined by the Ames assay. These results demonstrate the inability of NTOE to produce oral, dermal or mutagenic toxicity in animal models at doses greater than 300 times the normal human consumption of lycopene. Consumption analysis of lycopene-containing foods estimated mean daily intake of lycopene at 8.2mg/day.

Administration, Cutaneous↗

Lessons learned from process incident databases and the process safety incident database (PSID) approach sponsored by the Center for Chemical Process Safety.

Learning from the experiences of others has long been recognized as a valued and relatively painless process. In the world of process safety, this learning method is an essential tool since industry has neither the time and resources nor the willingness to experience an incident before taking corrective or preventative steps. This paper examines the need for and value of process safety incident databases that collect incidents of high learning value and structure them so that needed information can be easily and quickly extracted. It also explores how they might be used to prevent incidents by increasing awareness and by being a tool for conducting PHAs and incident investigations. The paper then discusses how the CCPS PSID meets those requirements, how PSID is structured and managed, and its attributes and features.

Accident Prevention↗

Jarosite characteristics and its utilisation potentials.

During metallic zinc extraction from zinc sulphide or sulphide ore, huge quantity of jarosite is being released universally as solid residues. The jarosite mainly contains iron, sulphur, zinc, calcium, lead, cadmium and aluminium. Jarosite released from such industrial process is complex and its quality and quantity make the task more complex for safe disposal. Apart from water contamination, jarosite already accumulated and its increasing annual production is a major source of pollution for surrounding environment including soil, vegetation and aquatic life and hence its disposal leads to major concern because of the stringent environmental protection regulations. An attempt was made to evaluate the characteristics of Indian jarosite with an objectives to understand its potentials for recycling and utilising as raw materials for developing value added products. Sand and Coal Combustion Residues (CCRs) was used as an admixture to attain good workability and detoxify the toxic substance in the jarosite. Result revealed that jarosite is silty clay loam in texture having 63.48% silt sized and 32.35% clay sized particles. The particle size of jarosite (D90=16.21+/-0.20 microm) is finer than the CCRs (D90=19.72+/-0.18 microm). The jarosite is nonuniform in structure and shape as compared to the CCRs having spherical, hollow shaped and some of them are cenosphere in nature. The major mineral phase of jarosite is Potassium Iron Sulphate Hydroxide {KFe3(SO4)2(OH)6}and Iron Sulphate Hydrate {2 Fe2O3SO3 x 5 H2O}. In CCRs the dominant phases are quartz {SiO2}, mullite {3 Al2O3 x 2 SiO2} and hematite {Fe2O3}. The high electrical conductivity of jarosite (13.26+/-0.437 dS/m) indicates that the presence of cations and anions are predominant over CCRs (0.498+/-0.007 dS/m). The major portion of jarosite consists of iron (23.66+/-0.18%), sulphur (12.23+/-0.2%) and zinc (8.243+/-0.075%). But CCRs main constituents are silicon (27.41+/-0.74%), aluminium (15.167+/-0.376%) and iron (4.447+/-0.69%). The other constituents such as calcium, aluminium, silicon, lead, and manganese are also present in the range of 0.5 to 5%. Heavy metals such as copper, chromium, and cadmium are found higher in jarosite as compared to the CCRs. The statistically designed experimental trials revealed that the density, water absorption capacity and compressive strength of fired jarosite bricks are 1.51 gm/cm3, 17.46% and 43.4 kg/cm2 respectively with jarosite sand mixture in the ratio of 3:1 indicating the potentials in developing building materials.

Coal↗

Hypersensitivity pneumonitis due to inhalation of fungi-contaminated esparto dust in a plaster worker.

Hypersensitivity pneumonitis or extrinsic allergic alveolitis can be defined as a lung disease caused by a wide group of antigens that reach the lung by inhalation of organic and/or inorganic dust of various sources. The esparto (Stipa Tenacissima and Ligeum Spartum) is an herbaceous of the grass family used in the production of ropes, canvas, sandals, mats, baskets, and so forth. It is also used in the construction industry for the production of paper paste. Inhalation of esparto dust has been reported as cause of hypersensitivity pneumonitis. The existence of precipitating antibodies against esparto extract has been proved. During the esparto fiber manufacturing process, esparto grass can be contaminated by moulds and thermophilic actinomycetes, which have been described as the causing antigens of hypersensitivity pneumonitis in plaster workers. We present a case of occupational hypersensitivity pneumonitis in a plaster worker. Clinical findings, precipitating antibodies, and evolution, after having removed him from his work, confirmed the diagnosis. In our case, Aspergillus species contaminating esparto are probably the antigens that caused the disease.

Adult↗

A multivariate approach to the study of the composting process by means of analytical electrofocusing.

Three blends formed by: agro-industrial waste, wastewater sewage sludge, and their mixture, blended with tree pruning as bulking agent, were composted over a 3-month period. During the composting process the blends were monitored for the main physical and chemical characteristics. Electrofocusing (EF) was carried out on the extracted organic matter. The EF profiles were analyzed by principal component analysis (PCA) in order to assess the suitability of EF to evaluate the stabilisation level during the composting process. Throughout the process, the blends showed a general shifting of focused bands, from low to high pH, even though the compost origin affected the EF profiles. If the EF profile is analyzed by dividing it into pH regions, the interpretation of the results can be affected by the origin of compost. A good clustering of compost samples depending on the process time was obtained by analyzing the whole profile by PCA. Analysis of EF results with PCA represents a useful analytical technique to study the evolution and the stabilisation of composted organic matter.

Animals↗

Interaction forces in bitumen extraction from oil sands.

Water-based extraction process (WBEP) has been successfully applied to bitumen recovery from Athabasca oil sand ore deposits in Alberta. In this process, two essential steps are involved. The bitumen first needs to be "liberated" from sand grains, followed by "aeration" with air bubbles. Bitumen "liberation" from the sand grains is controlled by the interaction between the bitumen and sand grains. Bitumen "aeration" is dependent, among other mechanical and hydrodynamic variables, on the hydrophobicity of the bitumen surface, which is controlled by water chemistry and interactions between bitumen and fine solids. In this paper, the interaction force measured with an atomic force microscope (AFM) between bitumen-bitumen, bitumen-silica, bitumen-clays and bitumen-fines is summarized. The measured interaction force barrier coupled with the contacted adhesion force allows us to predict the coagulative state of colloidal systems. Zeta potential distribution measurements, in terms of heterocoagulation, confirmed the prediction of the measured force profiles using AFM. The results show that solution pH and calcium addition can significantly affect the colloidal interactions of various components in oil sand extraction systems. The strong attachment of fines from a poor processing ore on bitumen is responsible for the corresponding low bitumen flotation recovery. The identification of the dominant non-contact forces by fitting with the classical DLVO or extended DLVO theory provides guidance for controlling the interaction behavior of the oil sand components through monitoring the factors that could affect the non-contact forces. The findings provide insights into megascale industrial operations of oil sand extraction.

Journal Article↗

[Protein concentrate of African oil palm (Elaesis guineensis, Jacquin), extraction process and functional properties].

A study was carried out for the purpose of obtaining and characterizing a protein concentrate obtained from defatted oil palm cake using alkaline extraction, and compare it with a commercial soy meal. The oil palm cake came from a national industry as a subproduct of the oil extraction of the palm kernels. The moisture, protein, fat, crude fiber and ash content of the oil palm was then determined. The optimum conditions for extraction and precipitation of the proteins were selected. These were the following: extraction at pH, 11.4; adding NaOH 0.06 M solvent; a meal/solvent relation of 1:20 g/ml and extraction time, 20 minutes with magnetic agitation, and precipitation at pH 5.3. The protein concentrate obtained contained: 66.50% protein; 0.07% fat, 0.90% crude fiber, and 3.20% ashes. Then the following functional properties were analyzed: solubility, according to the pH; water absorption (250); oil absorption (175); emulsion activity (27.2), and stability (13.6). The author concludes that the protein concentrate has good water and oil absorption when compared to soymeal; the emulsion, however, was found to be unstable to heat.

Emulsions↗

Integrated bioprocesses.

Integrated bioprocesses have been developed to optimise yield and cost-effectiveness of production of low and high molecular weight molecules. Low molecular weight products are removed from the cultivation medium with in situ extraction, in situ adsorption or crystallisation to avoid product inhibition. One-pot processes are being developed to replace two-stage reactions. Recent developments in the integrated purification of high molecular weight products focus mainly on the integration of solid/liquid separation and initial product recovery such as expanded bed adsorption or extraction in aqueous two-phase systems. Additionally, new approaches for a more efficient processing of inclusion bodies have been developed.

Bacteria↗

Lead removal from foundry waste by solvent extraction.

Solvent extraction is used to reduce lead concentrations from millpond wastewater solids, a type of foundry process waste. Toluene and toluene mixed with di-(2-ethyl-hexyl) phosphoric acid (HDEHP) have been tried as leaching solvents. Toluene is ineffective as a solvent in extracting lead, but the toluene-HDEHP mixture effectively removes lead from solid foundry waste. The effects of the HDEHP concentration, the contact time, and the amount of solvent used on lead extraction have been investigated. The mass transfer process is rapid: contact time of 1/2 hour has been found to be sufficient to accomplish the leaching process. The concentration of HDEHP significantly impacts lead removal. The optimum concentration of HDEHP is determined to range from 0.05 to 0.1 mol/l. The Toxicity Characteristic Leaching Procedure (TCLP) test of the treated samples gives leachable lead in much lower quantities than those found in the untreated samples. Thus the solvent extraction process appears to be an effective method to significantly reduce the lead content of millpond wastewater solids.

Industrial Waste↗

Compounds of parasitic roundworm absorbing in the visible region: target molecules for detection of roundworm in Atlantic cod.

The objective of this study was to contribute to the development of technology that will be able to replace manual operations in processing of fish fillets. Removal of parasites, black lining, remnants of skin, and bloodstains are costly and time-consuming operations to the fish processing industry. The presence of parasites in fish products tends to spoil consumers' appetites. Recent reports questioning the safety of eating cod infected with parasites might lower consumer acceptance of seafood. Presently, parasites are detected and removed manually. An average efficiency of about 75% under commercial conditions has been reported. In this study, we focused on biochemical differences between cod muscle and the prevalent anisakine nematode species (Anisakis simplex and Pseudoterranova decipiens) infecting Atlantic cod (Gadus morhua). Using reversed phase high-performance liquid chromatography equipped with a photodiode array detector, substances absorbing in the range 300 to 600 nm were identified in extracts from parasite material. These substances were not detected in extracts from cod tissue. Significant biochemical differences between cod muscle and parasite material have thus been demonstrated.

Animals↗

Purification of glucose oxidase from Aspergillus niger by liquid-liquid cationic reversed micelles extraction.

The aim of this work was to select the operating conditions for the extraction and recovery of glucose oxidase (GOX) by reversed micelles from mixtures of commercial enzyme and Aspergillus niger homogenates. For this purpose, the influence of the main operating parameters (pH, surfactant concentration, and presence of cell debris or not) on GOX extraction was investigated at 25 degrees C. Without cell debris, the highest yield of GOX activity recovery (90.8%) was obtained performing (a) the forward extraction in isooctane as solvent and hexanol and butanol as cosolvents at 76/6/18 ratio, pH 7.0, 0.2 M cetyl trimethylammonium bromide as cationic surfactant, and electric conductivity of 5.0 mS cm(-1) and (b) the backward extraction at pH 5.5. Forward and backward extractions furnished comparable results when using raw homogenate, which demonstrates a negligible impact of the presence of cell debris on the process. The highest extraction yield (94%) was obtained under the same forward and backward conditions adopted without cell debris. The promising results of this work suggest that the proposed methodology could be profitably exploited at an industrial level.

Aspergillus niger↗

Investigation of polycyclic aromatic hydrocarbons (PAHs) in soil at Agra, India--a case study.

Polycyclic Aromatic Hydrocarbons (PAHs) are released into the environment from anthropogenic sources, such as combustion of fossil fuels, refused burning, industrial processes and motor vehicle exhausts. The concentration of PAHs in roadside soil was measured at St. John's crossing, which lies in the centre of Agra city and exposed to heavy traffic. The samples were extracted with hexane by ultrasonic agitation. The extracts were then fractioned on a silica-gel column and the aromatic fraction was subjected to HPLC for analysis of 16 priority PAH pollutants specified by environment protection agency (EPA). Total mean concentration of PAHs was found to be 15.29 microg g(-1) and it ranged from 6.72-25.91 microg g(-1). Fluoranthene, chrysene, benzo(b)fluoranthene and benzo(ghi)perylene were found to be the most abundant PAHs at this location.

Chromatography, High Pressure Liquid↗

Purification of catalase from human placenta.

The therapeutic use of an antioxidant complex containing superoxide dismutase and catalase has been proposed for the treatment of several diseases in which reactive oxygen species have an important role. Although superoxide dismutase for human use is commercially available, methods for the production of catalase for human use have not been described. An industrial process was developed for the purification of catalase for human use as a by-product of albumin production from human placenta, comprising two parts: (1) albumin and catalase co-purification steps, including blood extraction from ground placentas, precipitation of haemoglobin with ethanol/chloroform, concentration/diafiltration by tangential filtration and anionic chromatography, by which non-adsorbed catalase was separated from albumin; and (2) catalase purification steps after albumin separation, including a second anionic chromatography step and dye-affinity chromatography. This method provided a final recovery of 27% (70-100% in each step) with 670-fold purification of catalase (85% pure) and a specific activity of 49000 units/mg, which is higher than that of commercially available human catalase. This process permits the co-purification of catalase and albumin and can easily be scaled up.

Catalase↗