Question: I do not know how 0.00360 kg H20 calculated. This is for input and output. Be thorough to the fullest. Eliminating discharges of hot streams

I do not know how 0.00360 kg H20 calculated. This is for input and output. Be thorough to the fullest. I do not know how 0.00360 kg H20 calculated. This is for

Eliminating discharges of hot streams to the environment has two beneficial effects: the temperature of the receiving entity (c.g. a lake, a river, or the atmosphere) is not raised, which can avoid violating an EPA rogulation, and the escrgy contained in the discharged stream is nos wasted by being dissipated in the environmemt. For example, a gas stream at 500C containing 8.0 mol CO and 92.0CO, hat was originally going to be sent up a stack is instead semt to a heat exchanger and flows across tubeshinough which water is flowing. The suater enters at 25C and is fed at a ratio of 0.200mol water/mol hot gas, is heared to its boiling point, and forms saturated steam at 5.0 bar. The steam may be used for heating or power generation in the plant or as the feed to another process unit. The beat exchanger can be assumed to operate adiabatically -that is, all beat transferred from the hot gas goes wo beat the waver, as opposed to some of it leaking through the beat exchanser walls to the environment. The flowchart for an assumed basis of L00 mall fuesi susis shown below. Eliminating discharges of hot streams to the environment has two beneficial effects: the temperature of the receiving entity (c.g. a lake, a river, or the atmosphere) is not raised, which can avoid violating an EPA rogulation, and the escrgy contained in the discharged stream is nos wasted by being dissipated in the environmemt. For example, a gas stream at 500C containing 8.0 mol CO and 92.0CO, hat was originally going to be sent up a stack is instead semt to a heat exchanger and flows across tubeshinough which water is flowing. The suater enters at 25C and is fed at a ratio of 0.200mol water/mol hot gas, is heared to its boiling point, and forms saturated steam at 5.0 bar. The steam may be used for heating or power generation in the plant or as the feed to another process unit. The beat exchanger can be assumed to operate adiabatically -that is, all beat transferred from the hot gas goes wo beat the waver, as opposed to some of it leaking through the beat exchanser walls to the environment. The flowchart for an assumed basis of L00 mall fuesi susis shown below

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