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The heating duty requirements for each case are calculated.
The evaluation results indicate the heating duty reduction of 56.8% from the proposed process over the conventional process and 64.6% reduction of cooling duty.
The heating duty of the proposed DWC including tray heat transfer is 35% less than that of the conventional system, and the cooling duty is 18% less.
If a feed is excessively sub-cooled, the stage-H plots show a sharp enthalpy changes on the reboiler side, and extent of this change determines the approximate feed heating duty required.
Feed conditioning is necessary when sharp enthalpy change in reboiler or condenser is noticed on the stage-H CGCC plot: If a feed is excessively sub-cooled, the stage-H plots show a sharp enthalpy changes on the reboiler side, and extent of this change determines the approximate feed heating duty required.
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However, re-use of hot oil between different heating duties enables hot oil networks to be designed with series arrangements.
Details of energy accounting on cooling and heating duties of key distillation towers, auxiliary heat exchanger duties, and power consumption for compressor system are provided for each start-up case.
Breweries require steam for various heating duties.
The main goal is to reduce the condenser heat duty.
The process gain varies in sign with the reboiler heat duty due to mass transfer effects.
This chapter concentrates on basic heat transfer theory and process heat duty.
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