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Titlebook: Applied Chemical Process Design; Frank Aerstin,Gary Street Book 1978 Plenum Press, New York 1978 design.development.engine.engineering des

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發(fā)表于 2025-3-21 16:05:33 | 只看該作者 |倒序?yàn)g覽 |閱讀模式
期刊全稱Applied Chemical Process Design
影響因子2023Frank Aerstin,Gary Street
視頻videohttp://file.papertrans.cn/160/159673/159673.mp4
圖書封面Titlebook: Applied Chemical Process Design;  Frank Aerstin,Gary Street Book 1978 Plenum Press, New York 1978 design.development.engine.engineering des
影響因子Development of a new chemical plant or process from concept evaluation to profitable reality is often an enormously complex problem. Generally, a plant-design project moves to completion through a series of stages which may include inception, preliminary evaluation of economics and market, data development for a final design, final economic evaluation, detailed engineering design, procurement, erection, startup, and pro- duction. The general term plant design includes all of the engineering aspects involved in the development of either a new, modified, or expanded industrial plant. In this context, individuals involved in such work will be making economic evaluations of new processes, designing individual pieces of equipment for the proposed new ventures, or developing a plant layout for coordination of the overall operation. Because of the many design duties encountered, the engineer involved is many times referred to as a design engineer. If the latter specializes in the economic aspects of the design, the individual may be referred to as a cost engineer. On the other hand, if he or she emphasizes the actual design of the equipment and facilities necessary for carrying out the pr
Pindex Book 1978
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Safety Relief Valves and Rupture Disks,nvolve complex two-phase flow calculations, which are beyond the scope of this work. In fact, the entire area of emergency relief systems is undergoing study which will result in changes in the calculational procedures. This work is being done by the Design Institute for Emergency Relief Systems (DI
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https://doi.org/10.1007/978-3-030-74490-8 shaped particles is.Depending on the size of the particle, various forms of Equation (7.1) are used to calculate the actual terminal velocity. Figure 7.1 summarizes the equations and their application.
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https://doi.org/10.1007/978-3-031-21398-4from the low absolute pressure at the suction to a higher pressure at the discharge. The ratio of discharge pressure over suction pressure (ratio of compression) is about 6 or 10 to 1, per stage. As with other types of gas compressors, the compression stages are operated in series to obtain a greater overall compression, or lower suction pressure.
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Gas-Solid Separations, shaped particles is.Depending on the size of the particle, various forms of Equation (7.1) are used to calculate the actual terminal velocity. Figure 7.1 summarizes the equations and their application.
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