By Stanley M. Walas
Chemical strategy apparatus is a consultant to the choice and layout of quite a lot of chemical strategy apparatus. Emphasis is put on particular details in regards to the approach layout and function of kit. To this finish, recognition is given to examples of profitable functions, and a beneficiant variety of line sketches displaying the functioning of apparatus is integrated with many graphs and tables giving their real functionality. For coherence, short stories of perininent thought, together with numerical examples to demonstrate the extra concerned systems, are supplied in key chapters.
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Additional resources for Chemical process equipment: selection and design
Lund, Industrial Pollution Control Handbook, McGraw-Hill, New York, 1971. 5. Rosaler and Rice, Standard Handbook of Plant Engineering, McGraw-Hill, New York, 1983. 6. Sax, Dangerous Properties of Industrial Materials, Van Nostrandl Reinhold, New York, 1982. 7. Wells, Safety in Process Plant Design, George Godwin, Wiley, New York, 1980. 2. Process Equipment A. Encyclopedias 1. Considine, Chemical and Process Technology Encyclopedia, McGrawHill, New York, 1974. 2. Kirk-Othmer Concise Encyclopedia of Chemical Technology, Wiley, New York, 1985.
The feed and hot well pumps make the net power production 4700 kW. Conditions at 11 key points are indicated on the enthalpy-entropy diagram. The process steam is extracted from the turbine at an intermediate point, while the rest of the stream expands to 1in. 48, McGraw-Hill, New York, 1973). 1u. 838 FRACTIONATOR SIDESTREAM 17,300pph 580 F whose main function is to supply heat to crude topping and vacuum service in a 20,00OBbl/day plant. (a) Recovery of heat from a sidestream of a fractionator in a 9000 Bbl/day fluid catalytic cracker by generating steam, Q = 15,950,000Btu/hr.
The 2. CRACKING OF GAS A gas oil cracking plant consists of two cracking furnaces, a soaker, a main fractionator, and auxiliary strippers, exchangers, pumps, and drums. The main fractionator (15Opsig) consists of four zones, the bottom zone being no. 1. A light vacuum gas oil (LVGO) is charged to the top plate of zone 3, removed from the bottom tray of this zone and pumped to furnace no. 1 that operates at 1OOOpsig and 1000°F. 1 bottoms is pumped to storage. The overhead is cooled in a water exchanger and proceeds to a separating drum.