Introduction to process engineering and design by Thakore

By Thakore

Advent to method engineering and layout

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After the reaction, excess hydrogen is recycled from the separation unit back to the reaction unit. For recovery of volatile organic compounds (VOC) from vent gases, carbon adsorption units are commonly employed. Nitrogen is used for regeneration of the carbon bed from which VOC is separated. VOC laden nitrogen is recycled. Other reasons for recycle are utilization of heat from the outgoing stream, to improve the performance of an equipment, to improve selectivity of a product, to improve safety of the process, to minimize waste generation, etc.

End use of treated water is a chief governing factor in deciding the process steps to be selected. Production of drinking water demands different steps as compared to production of high quality water for boiler feed (BF) make-up purpose. Drinking water requirements can be met by different water treatment steps. If water contains less dissolved solids, say less than 500 mg/L, clarification and disinfection by chlorination could be satisfactory. However, if raw water has high dissolved solids, dual filtration followed by desalination by reverse osmosis and pW adjustment would be necessary.

Further it is heated to 260oC with the reactor exit stream. Superheated ammonia at the rate of 3266 NnrVh and hot air at the rate of 29 394 NnvVh are fed to the reactor. 016 kg moisture/kg dry air. In the reactor, ammonia is completely consumed. Yields of NO, N2 and N20 are 95%, 2% and 3%, based on ammonia conversion. 5 bar g. Carry out the material and energy balances of the reactor system and preheating equipments. 44 kmol/h Assume dry air molar composition to be 21% 02, 1% Ar and 78% N2. 5474 Source of data: Ref.

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