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Fermentation pharmaceutical products

Membrane bioreactors have applications in fermentation, pharmaceutical production, protein extraction and wastewater treatment (Inloes et al., 1983 Gabelman and Hwang, 1999). Membranes can be used in the recycle loop with other types of reactor, such as CSTR, in which the membrane module is used to separate the cells from the product stream and then recycle the cells back into the reactor. In another arrangement, cells or enzymes can be entrapped on the surface of the membrane or incorporated into the membrane s porous structure. The substrate is fed through the lumen and product leaves the other side of the lumen through the shell side of the module. [Pg.193]

Pharmaceutical. Ion-exchange resins are useful in both the production of pharmaceuticals (qv) and the oral adrninistration of medicine (32). Antibiotics (qv), such as streptomycin [57-92-17, neomycin [1404-04-2] (33), and cephalosporin C [61-24-5] (34), which are produced by fermentation, are recovered, concentrated, and purified by adsorption on ion-exchange resins, or polymeric adsorbents. Impurities are removed from other types of pharmaceutical products in a similar manner. Resins serve as catalysts in the manufacture of intermediate chemicals. [Pg.387]

Pharmaceuticals. Pharmaceuticals account for 6% of the Hquid-phase activated carbon consumption (74). Many antibiotics, vitarnins, and steroids are isolated from fermentation broths by adsorption onto carbon foUowed by solvent extraction and distillation (82). Other uses in pharmaceutical production include process water purification and removal of impurities from intravenous solutions prior to packaging (83). [Pg.534]

Gas dispersion and blending for tall reactors Fermentations (food products, pharmaceuticals)... [Pg.567]

Fermentation broths are complex, aqueous mixtures of cells, comprising soluble extracellular, intracellular products and any unconverted substrate or unconvertible components. Recovery and extraction of product is important in bioprocess engineering. In particular separation is a useful technique it depends on product, its solubility, size of the process, and product value. Purification of high-value pharmaceutical products using chromatography such as hormones, antibody and enzymes is expensive and difficult to scale up.1 Tire necessary steps to follow a specific process depend on the nature of the product and the characteristics of the fermentation broth. There are a few steps for product recovery the following processes are discussed, which are considered as an alternative for product recovery from fermentation broth. [Pg.170]

The production of ethyl alcohol for beverage, cosmetic, and pharmaceutical products is commonly accomplished by the natural process of fermentation. See Ethyl Alcohol Methyl Alcohol and Fermentation, Beer, wine, and whiskey production are extensively covered in the Foods and... [Pg.47]

A broad spectrum of enzymes and fermentation systems has already become available to the industry, and the number is increasing all the time. Biotech development has also picked up speed it can now take a matter of weeks rather than years to develop new, highly specific and efficient enzymes. Until recently, slow development hindered the use of enzymes in pharmaceutical production. Now DSM s Pharmaceutical Product Unit, for example, is exploiting them systematically as a competitive advantage. Enzymes are also becoming more resistant to harsh environments such as heat and acidity, and are cheaper to produce, making inroads into other industrial production processes such as pulp and paper, oil exploration, and textile processing. [Pg.377]

Following the initial stages of product recovery from a fermentation broth, a number of purification stages will be required in all but the simplest industrial processes. In the case of high-purity pharmaceutical products, a large number of separation stages are usually required to remove all impurities from the desired final product. By identifying some difference between the product and its impurities, either physical or chemical, the desired bioseparation can be achieved. [Pg.649]

Excipients manufactured by fermentation processes, such as dextrose, citric acid, mannitol, and trehalose, should be specially controlled for endotoxin levels. Mycotoxin (highly toxic metabolic products of certain fimgi species) contamination of an excipient derived from natural material has not been specifically addressed by regulatory authorities. The German health authority issued a draft guideline in 1997 where a limit was specified for Aflotoxins Mi, Bi, and the sum of Bi, B2, Gi, and G2 in the starting material for pharmaceutical products. [Pg.1641]

Specifically, a new composition of matter (NCM) or new chemical compound prepared by synthetic methods is the primary area of interest. They may be made using synthetic methods or are isolated from natural sources such as plant or oceanic material or from fermentation broths. At times, a compound is known in an impure state that is unusable as a pharmaceutical product. If it is obtained in a purified state and meets the requirements of patentability, it can be claimed as a compound of a defined purity. [Pg.2607]

Phenoxyacetic acid was separated from fermentation fluids, crude phenoxymethyl penicillin and finished pharmaceutical products. Determinations of the separated acid were made by ultraviolet spectrophotometry or a bromometric titration using an amperometric end point 68. a study of phenoxyacetic acid in penicillin V by ultraviolet spectroscopy has been described recently 6,... [Pg.271]

Wastewater treatment is relatively simple in that the sole purpose is the degradation of all the organic species present in the liquid to remove both biological oxygen demand (BOD) and chemical oxygen demand (COD). Three-phase fluidization is also of interest for bioremediation of contaminated soils. Production of alcohols by fermentation (e.g., ethanol from glucose) has been practiced commercially. Other fermentation processes have been examined for production of enzymes, acetic acid, stem cells, monoclonal antibodies, antibiotics, and other pharmaceutical products. [Pg.1018]

Biotechnology products are pharmaceutical products prepared by industrial processes that involve the use of biological systems such as fermentation or tissue culture. For some industries, these processes involve the use of genetically engineered organisms. The preparation of products generally involves recombinant DNA, monoclonal antibody/hybridoma, continuous cell lines, and cellular therapy technology. [Pg.183]

After the era of Pasteur, biotechnology facilitated elaboration and further development of various manufacturing procedures. It led to the development of the fermentation industry, which promoted both food and pharmaceutical production, allowed the elaboration of antibiotics in 1940, a milestone in the history of mankind, and, finally, facilitated the production of vaccines, enzymes, amino acids, etc. [Pg.154]

Partition coefficients of solutes are influenced by aqueous-solution properties (pH, ionic strength) and the solvent (hydrophobicity, polarity). Partition coefficients are relatively insensitive to temperature or solute concentrations over the ranges normally used in fermentation-broth processing. Among the aqueous properties, the pH is one of the more important variables (particularly for weak bases and acids). Several primary and secondary metabolites, such as penicillin, are weak acids or bases, and the pH can be used to control and even reverse the distribution coefficient. A list of pharmaceutical products that are weak acids or bases and are extracted with solvent is given in Table 4. [Pg.61]

Biological pharmaceutical products manufactured by these methods include vaccines, immunosera, antigens, hormones, cytokines, enzymes and other products of fermentation (including monoclonal antibodies and products derived from r-DNA). [Pg.554]


See other pages where Fermentation pharmaceutical products is mentioned: [Pg.43]    [Pg.98]    [Pg.292]    [Pg.227]    [Pg.663]    [Pg.40]    [Pg.266]    [Pg.480]    [Pg.221]    [Pg.164]    [Pg.71]    [Pg.330]    [Pg.12]    [Pg.256]    [Pg.178]    [Pg.146]    [Pg.289]    [Pg.318]    [Pg.409]    [Pg.419]    [Pg.419]    [Pg.34]    [Pg.253]    [Pg.403]    [Pg.1056]    [Pg.199]    [Pg.294]    [Pg.66]    [Pg.130]    [Pg.177]    [Pg.183]   
See also in sourсe #XX -- [ Pg.318 ]

See also in sourсe #XX -- [ Pg.318 ]




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