A waste water thermal energy utilization method suitable for viscose staple fiber industry
A viscose staple fiber, industrial technology, applied in the field of waste water comprehensive utilization process, can solve the problems of insufficient utilization of residual heat energy, short heat exchange process, single layout, etc., achieve good social benefits and economic value, strong practicability, and save energy The effect of water resources
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Embodiment 1
[0051] The invention relates to a waste water thermal energy utilization method suitable for the viscose staple fiber industry. The process includes the treatment process of heat exchange and reuse of waste water in the production of viscose staple fiber, wherein the waste heat water includes a plasticizing tank Overflow water, in the prior art, the waste heat of the plasticizing tank overflow water usually adopts such as Figure 5 The heat exchange process shown is for processing. The temperature of the plasticizing tank overflow water from the plasticizing tank is 90-95°C. After simple heat exchange, the overflow water of the plasticizing tank still has residual heat, and the temperature is 70-80°C. , that is, it is discharged to the sewage station for treatment, and its heat energy has not been fully utilized. Therefore, the following heat exchange process is adopted in this embodiment, that is, cascade heat exchange is performed on the overflow water of the plasticizing tan...
Embodiment 2
[0053] The difference between this embodiment and Embodiment 1 is that in this embodiment, the step-by-step heat exchange of the plasticizing tank overflow water includes the step-by-step heat exchange of the plasticizing tank replenishment water, desulfurization liquid and holding water, and the processing steps as follows:
[0054] A: Set up a primary heat exchanger, respectively send the overflow water of the plasticizing tank and the supplementary water of the plasticizing tank to the primary heat exchanger for heat exchange treatment. After the heat exchange treatment, the obtained plasticizing tank supplementary hot water is sent to The plasticizing tank, the overflow low-temperature water obtained from the plasticizing tank is sent to the secondary heat exchanger to complete the operation of step B;
[0055] B: Send the desulfurization liquid used in the desulfurization station to the secondary heat exchanger, and use the overflow low-temperature water of the plasticizi...
Embodiment 3
[0059] The difference between this embodiment and Embodiment 1 is that in this embodiment, the step-by-step heat exchange of the plasticizing tank overflow water includes the step-by-step heat exchange of the plasticizing tank replenishment water, sodium sulfide bath liquid and holding water, and at the same time , There is a collection tank connected to the plasticizing tank, and its interior is separated into two partitions by an overflow plate, which are high temperature zone and low temperature zone.
[0060] The treatment steps of the plasticizing tank overflow water involved in this embodiment include:
[0061] (1) The plasticizing tank overflow water in the plasticizing tank overflows to the high temperature zone of the collection tank, and the temperature of the plasticizing tank overflow water is 95°C;
[0062] (2) The overflow water of the plasticizing tank with a temperature of 95°C in the high temperature zone and the replenishment water of the plasticizing tank wi...
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