Method for adjusting concentration of cooling water treatment agent in circulating cooling water system, method for recovering discharged cooling water, and treatment device for discharged cooling water
A technology of cooling water treatment and circulating cooling water, applied in water/sludge/sewage treatment, osmosis/dialysis water/sewage treatment, sterilization/microdynamic water/sewage treatment, etc., can solve the problems of increasing treatment costs, Achieve stable operation and reduce water treatment costs
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[0111] Example
[0112] Hereinafter, the present invention will be explained more specifically with examples, but the present invention is not limited to the following examples as long as it does not exceed the gist.
Example
[0113] [First Embodiment]
[0114] Using Chiba industrial water as raw water, the effluent from the cooling tower of the circulating cooling water system operating at a concentration rate of 3.5 times (hereinafter referred to as "drain water") is processed in the order of coarse filter, MF membrane device, and RO membrane device. Perform water recovery and return the recovered water to the circulating cooling water system.
[0115] In this circulating cooling water system, as a scale dispersant, a copolymer of acrylic acid and AMPM (acrylic acid: AMPM (molar ratio) = 70:30, weight average molecular weight 10,000, hereinafter referred to as "AA / AMPS") is added to make the system The internal concentration is 3mg / L, and at the same time as a slime control agent, according to the method of the first embodiment of International Publication WO2011 / 125762, a compound chlorine agent prepared using sodium hydroxide, sulfamic acid and sodium hypochlorite is added to make The system maintai...
Example
[0122] [First comparative example]
[0123] In addition to fixing the concentration of the scale dispersant in the circulating water cooling system to 3 mg / L, the concentration of the slime control agent is fixed to 2 mg / L in terms of the combined chlorine concentration, and the water recovery rate in the RO membrane is 65% Except for the treatment in the state, the same cooling water treatment and water recovery treatment as in the first embodiment were performed, and water was passed for 30 days in the same manner, and the pressure change of the RO membrane was investigated. 21 days after the start of operation, the operating pressure of the RO membrane exceeded 1.4 MPa, and the pump head with sufficient water volume could not be ensured, and it was necessary to clean after 30 days of running water.
[0124] In the first comparative example, in the cooling water treatment of the circulating cooling water system, a sufficient amount of scale dispersant concentration was set to 3 m...
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