Sunday, May 4, 2014

Modern biotechnology began with Pasteur

Membrane filtration in biotechnology
Modern biotechnology began with Pasteur's portal conagra production of lactic acid in 1857 and Fleming's discovery of penicillin in 1928. These milestones led the first wave of biotechnological processes which moved production of especially antibiotics and amino acids from laboratory to industrial scale. In the second wave of biotechnological processes were molecular technique used to recombine DNA. At the end of the millennium began the third and still current biotech wave: here replaced the chemical portal conagra processes that use C 2 / C 3-chemistry based on oil and gas, with biotechnological processes. The main properties of membranes in the biotech industry portal conagra are: Operation at low to moderate temperature, which ensures careful product handling. Use of selective separeringsmekanismer such. sifting, opløsningsdiffusion or ion exchange. They are easy to install due to modular design. They have reduced energy consumption compared to conventional evaporators and condensers. Integration of synergy portal conagra with such processes. separators and evaporators, which together result in improved operations.
The main membrane processes in the biotech industry are microfiltration (MF), ultrafiltration portal conagra (UF), nanofiltration (NF) and reverse osmosis (RO). The main functions portal conagra of these membrane processes are compared in Table 1
Use of membrane processes use of membrane processes for the production of bulk fermentation products have largely been established since 1970 and include bulk commodities such. amino acids, organic acids, antibiotics, enzymes, and biopolymers. In order to demonstrate the potential of the membrane process of the bulk fermentation process is the production of antibiotics have been chosen as an example (Figure 1). The first important application of membranes in the production of antibiotics, separating the antibiotics from the fermentation broth using the MF or UF. MF-/UF-membraner who reject the biomass and allow antibiotics to be brought into the permeate. To maximize the benefits of this process can diafiltreringsvand - high-quality water, which dilutes the feed - added. Modules with open channels is a robust and energy efficient solution to handle flows with medium and high viscosity of suspended matter such. the fermentation medium. Figure 2 shows an installation of these modules in the fermentation industry. After that, the UF permeate is concentrated by NF and RO. It provides concentrated antibiotics flows in an aqueous portal conagra phase, which may be useful in the direct reuse as diafiltreringsvand in the early MF-/UF-stadie. In the subsequent step is purified further, for example, antibiotics. absorption, precipitation and the extension of the solvents. By taking absorberingsvejen (Figure 1) can be used for absorbing RO as an initial concentration step before the evaporation. In addition, inddamperkondensatet from the stage of thermal concentration treated with RO to obtain purified process water, which can potentially be used. As the last option portal conagra in the taskbar may UF used before crystallization to remove pyrogenic and other impurities.
Future biorefineries Biorefineries are integrated biotech facilities to ensure full utilization of the feed to the simultaneous production of such. food, biofuels and biochemicals. Examples include the integrated production of biofuels and / or biopolymers / biochemicals from sugars and / or cellulosic feedstocks portal conagra in factories in the sugar / starch or paper mills. Depending on the raw material, for example. Biomass from wood or starch is the first step pre-treatment and conversion of raw material for sugar (Figure 3). Depending on the type of the saccharification step, in the case of the sugars must be polished before it is processed further. Disc stack centrifuges and decanters, together with MF or UF ensure an effective response. In addition, the UF is used to recover the enzymes used for the conversion, so that they can be recycled. If sugar concentrations are very low, it is possible portal conagra to use RDF to achieve a more energy efficient sugar content of 25-35 Brix. Sugar current can then be converted to the desired biofuels or biopolymers / biochemicals using fermentation. During the fermentation the UF or MF can be used to recover the fermentation products from the fermentation plant and hence prevent produktinhibitorer stop the fermentation. The concept of a bioreactor (MBR) can either be used in a method which makes use of side stream, or with diaphragms which are directly immersed in the fermentation plant. Where the method of side stream is well-founded, the approach of immersion still under development. Use of the MF or UF to this separation of the fermentation products from the fermentation medium results in the permeate stream containing the desired product combined with sugar. With NF you can separate the sugar from the fermentation product, eg. bio

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