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Production processes blending

Cotton linters or wood pulp are nitrated using mixed acid followed by treatment with hot acidified water, pulping, neutralization, and washing. The finished product is blended for uniformity to a required nitrogen content. The controlling factors in the nitration process are the rates of diffusion of the acid into the fibers and of water out of the fibers, the composition of mixed acid, and the temperature (see Cellulose esters, inorganic esters). [Pg.14]

A modem petroleum refinery is a complex system of chemical and physical operations. The cmde oil is first separated by distillahon into fractions such as gasoline, kerosene, and fuel oil. Some of the distillate fractions are converted to more valuable products by cracking, polymerization, or reforming. The products are treated to remove undesirable components, such as sulfur, and then blended to meet the final product specifications. A detailed analysis of the entire petroleum production process, including emissions and controls, is obviously well beyond the scope of this text. [Pg.518]

The single-component bacterial vaccines are listed in Table 15.1. For each vaccine, notes are provided of the basic material fkm which the vaccine is made, the salient production processes and tests for potency and for safety. The multicomponent vaccines that are made by blending together two or more of the single component vaccines are required to meet the potency and safety requirements for each of the single components that they contain. The best known of the combined bacterial vaccines is the adsorbed diphtheria, tetanus and pertussis vaccine (DTPerWac/Ads) that is used to immunize infants, and the adsorbed diphtheria and tetanus vaccine (DTWac/Ads) that is used to reinforce the immunity of school entrants. [Pg.310]

Figure 10.7 shows the extended RTN formulated for the benchmark problem. The production process includes diverging and converging material flows, flexible proportions of output goods (task Tj), cyclic material flows (recycling of output from task T3 into state Si), intermediate products which cannot be stored (state nodes S5, S9, S10, S12), and blending of products in task Ti 5. All processing tasks are operated batch-wise with lower and upper bounds on batch sizes. Batch sizes are... [Pg.229]

Containers, Closures, and Packaging Components Production and Process Controfa.-Mother Liquors, In-Process Blending/ Mixing, Validation of Process and Control Procedures, Reprocessing, Process Change, Impurities... [Pg.327]

Ensuring homogeneous mixing of the components (APIs and excipients) of a pharmaceutical preparation is a crucial prerequisite for obtaining proper solid dosages (tablets and capsules). Pharmaceutical manufacturers invest much time, labor and material resources in this process. Blending is intended to ensure uniform distribution of all components in the end products,so that each dose wiU contain the correct amount of the active ingredient. [Pg.478]

Wet Process Phosphoric Acid. A production process flow diagram is shown in Figure 8. Insoluble phosphate rock is changed to water-soluble phosphoric acid by solubilizing the phosphate rock with an acid, generally sulfuric or nitric. The phosphoric acid produced from the nitric acid process is blended with other ingredients to produce a fertilizer, whereas the phosphoric acid produced from the sulfuric acid process must be concentrated before further use. Minor quantities of fluorine, iron, aluminum, sUica, and uranium are usually the most serious waste effluent problems. [Pg.411]

Table 7.6 shows the solution of the refineries network using the SAA scheme with N = 2000 and N = 20000 where the proposed model required 790CPUs to converge to the optimal solution. In addition to the master production plan devised for each refinery, the solution proposed the amounts of each intermediate stream to be exchanged between the different processes in the refineries. The formulation considered the uncertainty in the imported crude oil prices, petroleum product prices and demand. The three refineries collaborate to satisfy a given local market demand where the model provides the production and blending level targets for the individual sites. The annual production cost across the facilities was found to be 6 650 868. [Pg.155]

A quantity of an appropriate sterilized placebo powder is blended with sterile excipients prior to filling (if needed) in a manner similar to the production process being simulated. The medium is passed through the run as though it were an actual product batch, and all routine procedures used in manufacture of a batch are performed. Once the medium has been processed, it is held for a period of time at least equal to that for aseptically produced materials. Any aseptic manipulations performed during and at the end of the hold period should be simulated hold times and product recalculation. [Pg.312]

A quantity of an appropriate sterilized placebo powder is blended with sterile excipients prior to filling (if needed), in a manner similar to the production process being simulated. [Pg.878]

One way to utilize a stabilizer Is illustrated In Figure 5, which is simply the Figure 4 process with the liquids from K and 4 diverted to a stabilizer. The stabilizer could be either refluxed or cold-feed, as a further variation. This process reduces the recycle load significantly in the two lower compression stages, as compared to the previous processes. This process also provides an additional control for the crude oil vapor pressure which can be independently varied, since the fractionator split can be controlled and the fractionator bottom product is blended with the crude stream. It may be desirable to blend this stream into separator 1... [Pg.82]

Vermouth is prepared from a base wine, extracting flavorants from herbs and spices in wine or a brandy mixture, blending the extract with the base wine, fortifying the mixture to the desired level, and finally maturing the prepared vermouth (Amerine et ah, 1980). The basic steps involved in a typical vermouth production process are illustrated in Fig. 8.1. [Pg.258]


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See also in sourсe #XX -- [ Pg.262 ]




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