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2.2. Three methods are used to simulate the cooling of mixed hydrocarbons with water: (1) simple heatx model; (2) Strict heatx model; (3) Two heater models connecting a heat flow strand. Hydrocarbon stream: Temperature: 200 C Pressure: 4 bar Flow rate: 10000 kg/HR Percent composition: 50 wt% benzene, 20% styrene, 20% ethylbenzene and 10% water Cooling water: Temperature: 20 C Pressure: 10 bar Flow rate: 50000 kg / HR Percentage composition: 100% water (1) Using the shortcut method of Heatx simulation: the vaporization fraction of hydrocarbon outlet is 0.1, and there is no pressure drop between the two streams Use the shortcut of heat-x module + design option to estimate the heat exchange area required by the heat exchanger. U methods uses the constant U value option to set an empirical value; 2.2. Three methods are used to simulate the cooling of mixed hydrocarbons with water: (1) simple heatx model; (2) Strict heatx model; (3) Two heater models connecting a heat flow strand. Hydrocarbon stream: Temperature: 200 C Pressure: 4 bar Flow rate: 10000 kg/HR Percent composition: 50 wt% benzene, 20% styrene, 20% ethylbenzene and 10% water Cooling water: Temperature: 20 C Pressure: 10 bar Flow rate: 50000 kg / HR Percentage composition: 100% water (1) Using the shortcut method of Heatx simulation: the vaporization fraction of hydrocarbon outlet is 0.1, and there is no pressure drop between the two streams Use the shortcut of heat-x module + design option to estimate the heat exchange area required by the heat exchanger. U methods uses the constant U value option to set an empirical value