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Formulation pilot plant

During process development, a model can be developed as soon as a conceptual flow sheet has been formulated. This model can be updated as more information about the process is obtained. Even at an early stage in the project, the model can be used to assess the preliminary economics of the process and the effect of technological changes on these economics. The model can aid in interpreting pilot-plant data and allows the study of many process alternatives. [Pg.72]

Pilot plant experiments represent an essential step in the investigation of a process toward formulating specifications for a commercial plant. A pilot plant uses the microkinetic data derived by laboratory tests and provides information about the macro kinetics of a process. Examples include the interaction of large conglomerates of molecules, macroscopic fluid elements, the effects of the macroscopic streams of materials and energy on the process, as well as the true residence time in the full-scale plant. [Pg.1035]

This chapter deals with sodium a-olefinsulfonate (AOS) and with sodium internal olefmsulfonate (IOS). AOS is a well-established product and is being applied in many household and industrial formulations. IOS of a sufficiently high quality has only recently been made on laboratory scale and pilot plant scale and has not yet been applied in commercial formulations. AOS and IOS have not only good wetting and detergency properties, but also good tolerance toward water hardness ions, a combination not always observed for other anionic surfactants. [Pg.364]

The main role of pilot plant is in the scale-up of polymer formulations from laboratory to full scale production and the development of new processes and techniques, including trials of new equipment. The laboratory is normally where the chemistry of new products and processes is investigated and established. When scale-up is contemplated, the use of commercial quality materials will normally be investigated, test procedures established and certain processing tolerances examined. An experienced chemist can frequently learn much on the laboratory scale that will indicate likely scale-up behaviour, but it is always prudent to then go through the pilot stage before embarking on full scale production. [Pg.455]

Model validation requires confirming logic, assumptions, and behavior. These tasks involve comparison with historical input-output data, or data in the literature, comparison with pilot plant performance, and simulation. In general, data used in formulating a model should not be used to validate it if at all possible. Because model evaluation involves multiple criteria, it is helpful to find an expert opinion in the verification of models, that is, what do people think who know about the process being modeled ... [Pg.48]

Feed grain size, in potassium chloride compaction, 20 621—622 Feed handling, in pilot plants, 19 466-467 Feed industry, solid formulated enzymes in, 10 273 Feeding equipment... [Pg.349]

The conversions, selectivities, and kinetics are ideally obtained in a small batch reactor, the operating conditions and catalyst formulation are determined from a bench-scale continuous reactor, the process is tested and optimized in a pilot plant, and finally the plant is constructed and operated. While this is the ideal sequence, it seldom proceeds in this way, and the chemical engineer must be prepared to consider aU aspects simultaneously. [Pg.6]

Formulation Characterization. Prior to using a new propellant formulation in pilot-plant or production studies, the material must be fully characterized and analyzed Theologically. Processability predictions may be extrapolated from this step. [Pg.178]

The physical properties and specifications for the manufactured formulations should match those established earlier by the product formulator, the pilot plant staff, and the quality control department. Therefore, the product manufactured on a large scale should possess the appropriate quality properties. [Pg.823]

There are several uses of tablet press instrumentation in the scale-up process itself. One of these involves obtaining a sample of the scale-up batch and compacting that sample on the pilot-plant or research instrumented tablet press on which the formulation has been previously evaluated. Similarity of the fingerprint or the various research plots (Heckel, force-displacement, radial vs. axial plots) is evidence that the scale-up batch is similar to the previously evaluated research batch [2]. [Pg.232]

The alternative would be to obtain a portion of the formulation, lake it back to the instrumented press used in the pilot plant or in R D, and perform the same evaluation as was performed on the smaller batches. By this technique, one can evaluate the scale-up process for all the other operations and then note any differences in performance on the production press. [Pg.232]

Even though the process development activities typically begin after the formulation has been developed, they may also occur simultaneously. The majority of the process development activities occur either in the pilot plant or in the pro-... [Pg.50]

The formulation, manufacturing process, analytical development, and long-term toxicology studies in animals are parallel to the clinical investigation (Table 1.1). Clinical trial materials should be developed, manufactured, tested, and released before conducting a phase I clinical trial. Process chemists may redesign the synthetic route for the dmg candidate to meet the requirements of large-scale production in a pilot plant. Preformulation scientists complete the activities of salt selection,... [Pg.10]

All of these applications use fixed-bed reactors, and, very importantly, all were scaled up from bench-scale pilot plant data. This successful scale-up experience with the ZSM-5 catalyst was an important consideration in formulating the MTG development strategy. [Pg.32]

The first pilot plant grafting that was run with the commercial 2000 A latex from B. F. Goodrich coagulated. We switched Run 17B formulation with the pentamine/peroxide initiator system to the persulfate initiator system, Run 26 (Table VII). Based on tensile impact data, No. 26 had almost the same impact resistance as No. 17B. [Pg.269]


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