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By Jin Rai Cho et al.

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Example text

5 shows all instrumentation, including indicators and transmitters. The clutter on the diagram is minimized by tabulating the design and operating conditions of the major equipment below the diagram. 6 represents a gas treating plant that consists of an amine absorber and a regenerator and their immediate auxiliaries. Internals of the towers are shown with exact locations of inlet and outlet connections. The amount of simp1e process may be instrumentation for such a surprising. On a completely finished diagram, every line will carry a code designation identifying the size, the kind of fluid handled, the pressure rating, and material specification.

Then the gas is dried in a system of two desiccant-filled vessels that are used alternately for drying and regeneration. Subsequently the gas is precooled in exchanger E-6 and charged to a low temperature fractionator. This tower has a reboiler and a top refluxing system. At the top the conditions are 28Opsig and -75°F. Freon refrigerant at -90°F is used in the condenser. The bottoms is recycled to the pyrolysis coil. The uncondensed vapor leaving the reflux accumulator constitutes the product of this plant.

Cities, temperatures, pressures, monetary values, and all pertinent physical properties unless they are standard and can be established from correlations. This information about properties applies also to products of item 1. Daily and seasonal variations of any data of items 1 and 2 and subsequent items of these lists. All available laboratory and pilot plant data on reaction and phase equilibrium behaviors, catalyst degradation, and life and corrosion of equipment. Any available existing plant data of similar processes.

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A Candidate of New Insensitive High Explosive by Jin Rai Cho et al.


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