A kind of treatment process of molasses alcohol waste liquid
A technology for molasses alcohol waste liquid and treatment process, which is applied in the field of treatment technology of molasses alcohol waste liquid, can solve problems such as easy coking of furnace tubes, and achieve the effects of solving easy coking, improving combustion rate and solving environmental protection problems.
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Embodiment 1
[0028] The molasses alcohol waste liquid is evaporated and concentrated by using a high-speed and low-temperature slow-fouling evaporation device for the molasses alcohol waste liquid.
[0029] What is used in this embodiment is a high-speed and low-temperature slow-fouling evaporation device for molasses alcohol waste liquid containing three evaporation units.
[0030] First use a high-pressure pump to pump the alcohol waste liquid into the first heater 11, feed fresh steam and the juice gas from the first flash evaporator 12, and send it to the heater 11 through the steam injector 4, and heat the waste liquid to 110°C. Then enter the first flash evaporator 12 for vapor-liquid separation, and the separated waste liquid returns to the first heater 11 for reheating, then enters the first flash evaporator 12 for vapor-liquid separation, reciprocating cycle, until the waste liquid reaches 25BX Enter the second effect, that is, enter the second evaporation unit; the evaporated and...
Embodiment 2
[0034] The molasses alcohol waste liquid is evaporated and concentrated by using a high-speed and low-temperature slow-fouling evaporation device for the molasses alcohol waste liquid.
[0035] What is used in this embodiment is a high-speed and low-temperature slow-fouling evaporation device for molasses alcohol waste liquid containing three evaporation units.
[0036] First use a high-pressure pump to pump the alcohol waste liquid into the first heater 11, feed fresh steam and the juice gas from the first flash evaporator 12, and send it to the heater 11 through the steam injector 4, and heat the waste liquid to 110°C. Then enter the first flash evaporator 12 for vapor-liquid separation, and the separated waste liquid returns to the first heater 11 for reheating, then enters the first flash evaporator 12 for vapor-liquid separation, reciprocating cycle, until the waste liquid reaches 25BX Enter the second effect, that is, enter the second evaporation unit; the evaporated and...
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