CN104030498B - A kind of electric power plant circulating water parallel seismic method method - Google Patents
A kind of electric power plant circulating water parallel seismic method method Download PDFInfo
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Abstract
本发明公开了一种电厂循环水旁流处理方法,其属于电厂循环水杀菌处理技术领域,其顺序为:先将循环水送入多介质过滤器中过滤;然后再进行超滤处理;再将超滤出水送入纳滤中进行处理;得到的无硬度的纳滤产水作为电解液送入电解槽中进行电解制取次氯酸钠,通过调整电解液流速和电解电压控制电解后的产水有效氯含量达到100mg/L以上;最后将得到的含有次氯酸钠的无硬度水溶液回输至循环水中。本发明方法利用循环水高水温、高含盐量等特点,将循环水进行电解制取次氯酸钠,高温和高盐分均有利于提高电解产生的有效氯产量,将富含次氯酸钠的循环水回补至循环水系统,实现循环水持续杀菌处理,有效减少微生物滋生对循环水系统的影响。The invention discloses a side-flow treatment method of circulating water in a power plant, which belongs to the technical field of sterilizing treatment of circulating water in a power plant. The ultrafiltration effluent is sent to the nanofiltration for treatment; the obtained non-hardness nanofiltration product water is sent to the electrolytic cell as the electrolyte for electrolysis to produce sodium hypochlorite, and the available chlorine in the produced water after electrolysis is controlled by adjusting the flow rate of the electrolyte and the electrolysis voltage. The content reaches more than 100mg/L; finally, the obtained hardness-free aqueous solution containing sodium hypochlorite is returned to the circulating water. The method of the present invention utilizes the characteristics of high water temperature and high salt content of the circulating water to electrolyze the circulating water to produce sodium hypochlorite. The circulating water system realizes continuous sterilization treatment of circulating water, effectively reducing the impact of microbial growth on the circulating water system.
Description
技术领域technical field
本发明涉及一种电厂循环水系统的杀菌处理技术,尤其是一种电厂循环水旁流处理方法。The invention relates to a sterilization treatment technology for a circulating water system of a power plant, in particular to a side-flow treatment method for the circulating water of a power plant.
技术背景technical background
电厂循环水系统是电厂耗水量最大的系统,由于循环水常年水温在10~40℃范围内,而且阳光充足,营养物质丰富,是细菌生长、繁殖的有利环境,循环水系统结垢、腐蚀和微生物滋生是循环水系统长期面临的主要问题。为降低循环水系统结垢风险,要严格控制循环水浓缩倍率,部分循环水作为排污水被排掉;为降低循环水微生物滋生造成的影响,需要定期对循环水进行杀菌灭藻处理,目前主要采用向循环水中投加杀菌剂进行处理,但杀菌剂的投加一般为间断式,不具有持续性,存在投加不及时,投加量不足和投加间断时间过长导致杀菌效果不佳等问题。The circulating water system of the power plant is the system with the largest water consumption in the power plant. Since the temperature of the circulating water is in the range of 10-40 ℃ all year round, and it is sunny and rich in nutrients, it is a favorable environment for the growth and reproduction of bacteria. The scaling, corrosion and Microbial growth is the main problem faced by circulating water systems for a long time. In order to reduce the risk of fouling in the circulating water system, the concentration ratio of circulating water must be strictly controlled, and part of the circulating water shall be discharged as sewage; in order to reduce the impact of microbial growth in the circulating water, it is necessary to regularly sterilize the circulating water. The treatment is carried out by adding fungicides to circulating water, but the addition of fungicides is generally intermittent and not continuous, and there are problems such as untimely dosing, insufficient dosage, and too long dosing intervals, resulting in poor bactericidal effects, etc. question.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种杀菌效果好、能有效提高循环水浓缩倍率的电厂循环水旁流处理方法。The technical problem to be solved by the invention is to provide a side-flow treatment method of circulating water in a power plant, which has good bactericidal effect and can effectively increase the concentration ratio of circulating water.
为解决上述技术问题,本发明采取的技术方案为:一种电厂循环水旁流处理方法,其关键技术在于:所述方法步骤如下:In order to solve the above-mentioned technical problems, the technical solution adopted by the present invention is: a method for treating the bypass flow of circulating water in a power plant, the key technology of which is: the steps of the method are as follows:
1)将循环水送入多介质过滤器中过滤,使过滤出水浊度在5NTU以下;1) Send the circulating water to the multi-media filter for filtration, so that the turbidity of the filtered water is below 5NTU;
2)将步骤(1)中得到的过滤出水送入超滤中处理,控制超滤回收水率为80%-95%;2) Send the filtered water obtained in step (1) to ultrafiltration for treatment, and control the water recovery rate of ultrafiltration to 80%-95%;
3)将步骤(2)中得到的超滤出水送入纳滤中进行处理,调整纳滤进水pH值在6.0-8.0之间,控制纳滤回收水率为70%-90%;3) Send the ultrafiltration effluent obtained in step (2) into the nanofiltration for treatment, adjust the pH value of the nanofiltration influent to 6.0-8.0, and control the nanofiltration water recovery rate to 70%-90%;
4)将步骤(3)中得到的无硬度的纳滤产水作为电解液送入电解槽中进行电解制取次氯酸钠,通过调整电解液流速和电解电压控制电解后的产水有效氯含量达到100mg/L以上;4) Send the non-hardness nanofiltration product water obtained in step (3) as the electrolyte into the electrolytic cell for electrolysis to produce sodium hypochlorite, and control the available chlorine content of the product water after electrolysis to 100mg by adjusting the flow rate of the electrolyte and the electrolysis voltage /L above;
5)将步骤(4)中得到的含有次氯酸钠的无硬度水溶液回输至循环水中;5) returning the hardness-free aqueous solution containing sodium hypochlorite obtained in step (4) to the circulating water;
所述电厂循环水补水为地表水、地下水或城市中水。The supplementary circulating water of the power plant is surface water, ground water or urban reclaimed water.
将所述步骤4)中得到的含有次氯酸钠的无硬度水溶液中的一部分用于超滤的定期杀菌处理。A part of the hardness-free aqueous solution containing sodium hypochlorite obtained in step 4) is used for periodic sterilization treatment by ultrafiltration.
所述步骤4)具体为:无硬度的纳滤产水作为电解液送入电解槽中进行电解制取次氯酸钠时,通过调整电解液流速和电解电压控制电解后的产水有效氯产量使循环水中的余氯量满足循环水在不同季节的杀菌要求,在循环水微生物滋生不严重时可以减少电解液,甚至间断运行电解槽,将纳滤产水直接回输至循环水即可。The step 4) is specifically: when the nanofiltration water without hardness is sent into the electrolytic cell as the electrolyte for electrolysis to produce sodium hypochlorite, the output of available chlorine in the water after electrolysis is controlled by adjusting the flow rate of the electrolyte and the electrolysis voltage to make the circulating water The amount of residual chlorine can meet the sterilization requirements of circulating water in different seasons. When the microbial growth in circulating water is not serious, the electrolyte can be reduced, and even the electrolytic cell can be run intermittently, and the nanofiltration water can be directly returned to the circulating water.
本发明采用上述技术方案取得的有益效果如下:The beneficial effect that the present invention obtains by adopting above-mentioned technical scheme is as follows:
(1)本发明方法利用循环水高水温、高含盐量等特点,将循环水进行电解制取次氯酸钠,高温和高盐分均有利于提高电解产生的有效氯产量,将富含次氯酸钠的循环水回补至循环水系统,不引入外来杂质,并实现循环水持续杀菌处理,有效减少微生物滋生对循环水系统的影响。(1) The method of the present invention utilizes the characteristics of high water temperature and high salt content of circulating water to electrolyze the circulating water to produce sodium hypochlorite. Replenish to the circulating water system without introducing foreign impurities, and realize continuous sterilization treatment of circulating water, effectively reducing the impact of microbial growth on the circulating water system.
(2)本发明方法充分利用了纳滤能够回收一价离子,对二价离子和有机物去除效果较好的特点,将循环水中的氯化钠、氯化钾等一价盐提纯用于电解制氯,并将循环水中的钙、镁、硫酸根、有机物等易造成循环水结垢、污堵的有害物质去除,可以有效提高循环水浓缩倍率,减少循环水排污水量,有效节约水资源。(2) The method of the present invention makes full use of the characteristics that nanofiltration can recover monovalent ions and has a good removal effect on divalent ions and organic matter, and purify monovalent salts such as sodium chloride and potassium chloride in circulating water for electrolysis Chlorine, and remove calcium, magnesium, sulfate, organic matter and other harmful substances in circulating water that are likely to cause scaling and fouling in circulating water, which can effectively increase the concentration ratio of circulating water, reduce the amount of sewage discharged from circulating water, and effectively save water resources.
具体实施方式detailed description
实施例1Example 1
(1)从电厂循环水塔中抽取循环水,并以100m3/h的流量送入多介质过滤器中进行过滤,所述多介质过滤器的直径为Φ3200,层高1200mm,其中石英砂800mm,无烟煤400mm,单台多介质过滤器出力为50 m3/h。出水浊度小于5NTU。电厂循环水水质情况见表1。(1) Extract the circulating water from the circulating water tower of the power plant, and send it to the multi-media filter for filtration at a flow rate of 100m 3 /h. The diameter of the multi-media filter is Φ3200, the layer height is 1200mm, of which the quartz sand is 800mm, The anthracite is 400mm, and the output of a single multimedia filter is 50 m 3 /h. The turbidity of the effluent is less than 5NTU. The water quality of circulating water in the power plant is shown in Table 1.
表1 循环水水质情况Table 1 Circulating water quality
(2)将步骤(1)中的过滤器出水送入超滤中进行处理,所述超滤的膜元件为外压式超滤膜,回收率为90%,超滤出水SDI小于4.0。(2) Send the effluent from the filter in step (1) to ultrafiltration for treatment. The membrane element of the ultrafiltration is an external pressure ultrafiltration membrane, the recovery rate is 90%, and the SDI of the ultrafiltration effluent is less than 4.0.
(3)将步骤(2)中得到的超滤出水加盐酸调整pH值为6.0-6.5,送入纳滤进行处理,所述纳滤为一级两段,回收率为75%。纳滤产水中的二价离子已都被去除,一价离子被浓缩,其水质情况见表2。(3) Add hydrochloric acid to adjust the pH value of the ultrafiltration water obtained in step (2) to 6.0-6.5, and send it to nanofiltration for treatment. The nanofiltration is one stage and two stages, and the recovery rate is 75%. The divalent ions in the nanofiltration product water have all been removed, and the monovalent ions have been concentrated. The water quality is shown in Table 2.
表2 纳滤产水水质情况Table 2 Water quality of nanofiltration product water
(4)将步骤(3)中得到的超滤产水送入电解槽中进行电解,电解槽进水即超滤产水水温为30℃-35℃,流量为60 m3/h,控制电解槽电压为180V,电解液的有效氯含量为120-140mg/L,电解后的电解液温升为2-4℃。(4) Send the ultrafiltration product water obtained in step ( 3 ) into the electrolytic cell for electrolysis. The cell voltage is 180V, the available chlorine content of the electrolyte is 120-140mg/L, and the temperature rise of the electrolyte after electrolysis is 2-4°C.
(5)将步骤(4)中得到的含有次氯酸钠的无硬度水溶液回输至循环水中;(5) returning the hardness-free aqueous solution containing sodium hypochlorite obtained in step (4) to circulating water;
连续旁流处理120小时后,经测定循环水中的余氯含量已达到0.5mg/L以上,起到了较好的杀菌效果。旁路后的出水无硬度和硫酸根,有利于进一步提高循环水浓缩倍率。After 120 hours of continuous bypass treatment, the residual chlorine content in the circulating water has reached above 0.5 mg/L, which has a good bactericidal effect. The effluent after the bypass has no hardness and sulfate radicals, which is beneficial to further increase the concentration ratio of circulating water.
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| KR101717109B1 (en) * | 2015-02-10 | 2017-03-16 | 엘지전자 주식회사 | Method for sterilizing a water supply apparatus |
| CN105016541B (en) * | 2015-07-29 | 2017-04-26 | 凯姆德(北京)能源环境科技有限公司 | Method for separating and recovering salts from high-salt wastewater |
| CN110028193B (en) * | 2019-03-20 | 2022-05-06 | 北京万邦达环保技术股份有限公司 | Waste water recycling system |
| CN110092455A (en) * | 2019-05-20 | 2019-08-06 | 浙江天行健水务有限公司 | Secondary water-supply is salt-free from sterilization method |
| CN116332389A (en) * | 2022-09-27 | 2023-06-27 | 青岛双瑞海洋环境工程股份有限公司 | High-salt wastewater treatment system |
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