A kind of recycling method of methanol protein comprehensive wastewater
A methanol protein and comprehensive wastewater technology, which is applied in general water supply conservation, chemical instruments and methods, applications, etc., can solve the problems of inability to realize recycling, low equipment use efficiency, substandard wastewater treatment, etc., to achieve resource recovery and utilization, The effect of improving production efficiency and reducing investment
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Embodiment 1
[0016] (1) Centrifuge the washing wastewater A generated in the methanol protein production process under the conditions of 18-30°C, feed rate 20T / h, and centrifugal force 13000-18000×g to obtain heavy phase sediment C and light phase liquid D respectively ;
[0017] (2) Concentrate the light phase liquid D obtained in step (1) by ultrafiltration to 1 / 5 of the volume of the light phase liquid D under the conditions of 18-30°C, flow rate 2T / h, and feed pressure 0.4-0.6Mpa, and separate Obtain concentrated liquid E and clear liquid F;
[0018] (3) Mixing the heavy phase sediment C obtained in step (1) and the concentrate E obtained in step (2) as raw materials for making organic fertilizer;
[0019] (4) Combine the supernatant F obtained in step (2) and the wastewater B produced during the post-treatment process of methanol protein extraction, perform reverse osmosis treatment at 18-30°C and a working pressure of 0.6-0.9MPa, and concentrate to 1 / 3 of the total volume of the cl...
Embodiment 2
[0021] (1) Transport the washing wastewater A produced in the methanol protein production process to the GEA disc high-speed centrifuge, and centrifuge at 18-30°C, feed rate 20T / h, centrifugal force 13000-18000×g, respectively Obtain heavy phase sediment C and light phase liquid D;
[0022] (2) Transfer the light phase liquid D obtained in step (1) to a 1000 molecular weight ultrafiltration system, and concentrate it into a light phase liquid by ultrafiltration under the conditions of 18-30°C, flow rate 2T / h, and feed pressure 0.4-0.6Mpa 1 / 5 of the volume of D, separated to obtain concentrate E and supernatant F; the described 1000 molecular weight ultrafiltration system is a prior art, such as the 1000 molecular weight ultrafiltration system produced by Luoyang Yangming Water Treatment Co., Ltd. SA-UF-9-225 Molecular weight ultrafiltration system;
[0023] (3) Mixing the heavy phase sediment C obtained in step (1) and the concentrate E obtained in step (2) as raw materials f...
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