Process and device for utilizing circulation water residual heat in production of coated controlled release fertilizer
A technology of coated controlled-release fertilizer and circulating water, which is applied in fertilization equipment, application, chemical industry, etc., can solve the problems of high energy consumption, restricting the promotion and application of controlled-release fertilizer, etc., so as to reduce the amount of circulating water, reduce equipment investment and Operating cost, water saving effect
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Embodiment 1
[0027] The waste heat recovery and utilization device of circulating water in the production of coated controlled-release fertilizer, such as figure 1 As shown, it includes a fluidized bed 1, a fan 2, a condenser 3, a preheater 4, waste heat recovery heating equipment 5, a circulating water pump 6 and a cooling tower 7. The air of the fluidized bed 1 is connected to the outlet of the solvent mixed gas through the fan 2, the condenser 3, the preheater 4 and the preheated gas inlet of the fluidized bed 1 to form a closed circuit; the part of the cooling circulating water of the condenser 3 is connected with the The waste heat recovery heating equipment 5 is connected to form a cycle, and part of the cooling circulating water is connected to the cooling water tower 7 through the circulating water pump 6 to form a cycle; the heating medium of the preheater 4 is connected to the waste heat recovery heating equipment 5 to form a closed circuit.
[0028] The process of using this dev...
Embodiment 2
[0034] The waste heat recovery and utilization device of circulating water in the production of coated controlled-release fertilizer, the structure is still as follows figure 1 Shown, but utilize this device to carry out the process of recycling water waste heat utilization in the production of coated controlled-release fertilizer and the difference of embodiment 1 is:
[0035] The step A: the flow rate of the mixed gas from the fluidized bed 1 is 100000m 3 / h, the temperature is 60°C, enter the condenser 3 through the fan 2 to condense to 30°C to recover part of the solvent, enter the preheater 4 to preheat to 70°C, and then enter the fluidized bed 1 for recycling.
[0036] The step B: In the condenser 3, the cooling circulating water inlet temperature is 30°C, and the flow rate is 300m 3 / h, 55% of which comes from the cooling tower 7, and the remaining 45% comes from the waste heat recovery heating equipment 5, the return temperature of the cooling circulating water is 35°...
Embodiment 3
[0040] The waste heat recovery and utilization device of circulating water in the production of coated controlled-release fertilizer, the structure is still as follows figure 1 Shown, but utilize this device to carry out the process of circulating water waste heat utilization in the production of coated controlled-release fertilizer and the difference of embodiment 1 or 2 is:
[0041] The step A: the flow rate of the mixed gas from the fluidized bed 1 is 300000m 3 / h, the temperature is 70°C, enter the condenser 3 through the fan 2 to condense to 40°C to recover part of the solvent, enter the preheater 4 to preheat to 80°C, and then enter the fluidized bed 1 for recycling.
[0042] The step B: In the condenser 3, the cooling circulating water inlet temperature is 35°C, and the flow rate is 1000m 3 / h, 65% of which comes from the cooling tower 7, and the remaining 35% comes from the waste heat recovery heating equipment 5, the return temperature of the cooling circulating wate...
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