Residual heat utilization method and apparatus in AC sponging agent drying system
A drying system and foaming agent technology, applied in heating devices, chemical instruments and methods, using non-combustion exothermic chemical reactions to generate heat, etc., can solve energy waste, waste heat utilization in the drying section, waste heat waste, etc. problems, to achieve the effect of reducing waste heat loss, obvious energy saving effect, and reduced steam consumption
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Embodiment 1
[0026] The steam sent from the heating pipeline, the pressure of the steam is 0.8MPa, and the temperature is 150°C, is transported to the air heater. After the steam heats the air in the air heater, the hot air enters the AC for foaming The feeding box of the agent, so as to dry the AC blowing agent. The steam turns into secondary steam after exothermic process in the air heater, and the secondary steam contains a large amount of uncondensed steam and hot water, and then the secondary steam enters the pressure regulating device to adjust the pressure of the steam, usually Adjust the pressure of the steam to 0.6MPa and the temperature to 120°C, then transport the steam with adjusted pressure to the condensation kettle of the condensation section of the AC foaming agent for heating to provide heat for the condensation reaction, and the temperature in the condensation reactor is 105 The temperature of the condensed water is about 95°C, and the condensed water generated after the ...
Embodiment 2
[0028] The steam sent from the heating pipeline, the pressure of the steam is 0.8MPa, and the temperature is 160°C, is sent to the air heater. After the steam heats the air in the air heater, the hot air enters the AC foaming agent The feeding box, so as to dry the AC blowing agent. The steam turns into secondary steam after exothermic process in the air heater, and the secondary steam contains a large amount of uncondensed steam and hot water, and then the secondary steam enters the pressure regulating device to adjust the pressure of the steam, usually Adjust the pressure of the steam to 0.6MPa and the temperature to 130°C, then transport the steam with the adjusted pressure to the condensation kettle in the condensation section of the AC foaming agent for heating to provide heat for the condensation reaction, and the temperature of the reactants in the condensation reactor The temperature of the condensed water is 106°C; the condensed water generated after the steam passes ...
Embodiment 3
[0030] The steam sent from the heating pipeline, the pressure of the steam is 0.8MPa, and the temperature is 170°C, is transported to the air heater. After the steam heats the air in the air heater, the hot air enters the AC for foaming The feeding box of the agent, so as to dry the AC blowing agent. The steam turns into secondary steam after exothermic process in the air heater, and the secondary steam contains a large amount of uncondensed steam and hot water, and then the secondary steam enters the pressure regulating device to adjust the pressure of the steam, usually Adjust the pressure of the steam to 0.6MPa and the temperature to 140°C, then transport the steam with the adjusted pressure to the condensation kettle of the condensation section of the AC foaming agent for heating to provide heat for the condensation reaction, and the temperature of the reactants in the condensation reactor The temperature of the condensed water is 104°C; the condensed water generated after...
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