CN111892238A - A combined emergency treatment method for black and odorous water with forward osmosis-coagulation-anoxic hydrolysis - Google Patents
A combined emergency treatment method for black and odorous water with forward osmosis-coagulation-anoxic hydrolysis Download PDFInfo
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/445—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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Abstract
Description
技术领域technical field
本发明属于环境工程技术领域,具体涉及一种黑臭水正渗透-混凝-缺氧水解组合应急处理方法。The invention belongs to the technical field of environmental engineering, and in particular relates to a combined emergency treatment method of black and odorous water with forward osmosis-coagulation-anoxic hydrolysis.
背景技术Background technique
由于工业废水和生活污水的排放,城市河流、湖泊等地表水体的生态系统面临着重大的挑战,黑臭已成为我国很多城市普遍存在的问题。黑臭的形成机理是当水体遭受严重有机污染时,有机物的好氧分解使水体中耗氧速率大于复氧速率,造成水体缺氧,致使有机物降解不完全、速度减缓,厌氧生物降解过程生成硫化氢、胺、氨、硫醇等发臭物质,同时形成FeS、MnS等黑色物质,致使水体发黑发臭。Due to the discharge of industrial wastewater and domestic sewage, the ecosystems of urban rivers, lakes and other surface water bodies are facing major challenges. Black and odor has become a common problem in many cities in my country. The formation mechanism of black odor is that when the water body suffers from serious organic pollution, the aerobic decomposition of organic matter makes the oxygen consumption rate in the water body greater than the reoxygenation rate, resulting in anoxic water body, resulting in incomplete degradation of organic matter, slowing down, and anaerobic biodegradation process. Hydrogen sulfide, amine, ammonia, mercaptan and other odorous substances, and at the same time form black substances such as FeS, MnS, etc., causing the water body to become black and odorous.
目前关于黑臭水的治理方法包括物理法,化学法和生物法等。其中物理法包括调水、清淤等水利工程,以及机械除藻、引水稀释等,其主要问题是治标不治本,不能从根本上解决黑臭问题;化学法包括加入化学试剂除藻、加入铁盐除磷等,但化学试剂投加量大,成本较高;生物法应用较为广泛,受污染河流的原位生态修复技术包括曝气充氧、微生物修复、原生动物修复、植物修复及人工湿地修复等,生物法经济实用,但收效较慢,且植物受季节性影响明显。专利201611166004.2公布的《黑臭水A/O正渗透处理系统及处理工艺》将正渗透技术应用于黑臭水,但其先驱预处理技术包括臭氧氧化、空气吹脱、水解酸化、好氧生物流化床等组合技术,工艺复杂,且黑臭水相比污水有机负荷低,较难直接采用生化工程处理。如何充分发挥正渗透技术优势,对合理将其应用于黑臭水的治理起着至关重要的作用。At present, the treatment methods for black and odorous water include physical methods, chemical methods and biological methods. Among them, the physical method includes water conservancy projects such as water transfer and dredging, as well as mechanical algae removal, water diluting and dilution, etc. The main problem is to treat the symptoms rather than the root cause, and cannot fundamentally solve the problem of black and odor; chemical methods include adding chemical reagents to remove algae, adding iron Salt and phosphorus removal, etc., but the dosage of chemical reagents is large and the cost is high; biological methods are widely used, and the in-situ ecological restoration technologies of polluted rivers include aeration and oxygenation, microbial restoration, protozoa restoration, phytoremediation and constructed wetlands The biological method is economical and practical, but the effect is slow, and the plants are obviously affected by the season. "Black and odorous water A/O forward osmosis treatment system and treatment process" published by patent 201611166004.2 applies forward osmosis technology to black and odorous water, but its pioneer pretreatment technologies include ozone oxidation, air stripping, hydrolysis and acidification, aerobic biological flow Combination technologies such as chemical bed, the process is complex, and the organic load of black and odorous water is lower than that of sewage, so it is difficult to directly use biochemical engineering treatment. How to give full play to the advantages of forward osmosis technology plays a vital role in rationally applying it to the treatment of black and odorous water.
发明内容SUMMARY OF THE INVENTION
本发明针对当前黑臭水处理投入大、收效慢以及治标不治本易反复等问题,提出一种黑臭水正渗透-混凝-缺氧水解组合应急处理方法,以实现黑臭水应急处理的快速、稳定、长效目标。The present invention proposes a combined emergency treatment method for black and odorous water with positive osmosis-coagulation-anoxic hydrolysis in order to solve the problems of large investment, slow effect, and easy repetition of the symptoms, so as to realize the emergency treatment of black and odorous water. Fast, stable, long-term goals.
为达到上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种黑臭水正渗透-混凝-缺氧水解组合应急处理方法,包括如下步骤:A forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method for black and odorous water, comprising the following steps:
1)黑臭水首先通过梯级正渗透进行三级浓缩处理,三级汲取液渗透稀释后送入二级正渗透继续汲取操作,最后送入一级正渗透进行黑臭水浓缩,一级稀释汲取液再送入反渗透单元浓缩后返回三级正渗透系统循环使用;1) The black and odorous water is firstly subjected to three-level concentration treatment through stepped forward osmosis. The third-level drawing liquid is osmotically diluted and sent to the second-level forward osmosis to continue the drawing operation. Finally, it is sent to the first-level forward osmosis for black and smelly water concentration, and the first-level dilution and drawing The liquid is sent to the reverse osmosis unit for concentration and returned to the three-stage forward osmosis system for recycling;
2)黑臭水浓缩液进入混凝沉淀处理装置去除铁、锰及水中悬浮物、胶体物质;2) The black and odorous water concentrate enters the coagulation and sedimentation treatment device to remove iron, manganese and suspended solids and colloidal substances in water;
3)黑臭水浓缩液再送入生物膜缺氧池进行缺氧水解,提高浓缩水可生化性,降低有机负荷,出水最终排入市政污水管网送污水厂进行集中处理。3) The black and odorous water concentrate is sent to the biofilm anoxic tank for anoxic hydrolysis to improve the biodegradability of the concentrated water and reduce the organic load. The effluent is finally discharged into the municipal sewage pipe network and sent to the sewage plant for centralized treatment.
进一步的,所述步骤1)中,一级、二级正渗透浓缩倍数均采用2倍,三级正渗透浓缩倍数采用3倍,黑臭水经梯级浓缩后减容12倍,主要污染物浓度提高10倍左右,便于下一步高效处理。Further, in the step 1), the concentration ratio of the primary and secondary forward osmosis is 2 times, the concentration ratio of the tertiary forward osmosis is 3 times, and the black and odorous water is reduced by 12 times after the stepwise concentration, and the concentration of the main pollutants is 2 times. It is increased by about 10 times, which is convenient for efficient processing in the next step.
进一步的,所述步骤1)中,正渗透汲取液采用无机盐系汲取液,三级汲取液初始浓度为2M,可以确保汲取液进入一级正渗透系统时浓度达到0.5M,对黑臭水依然具有良好的浓缩效果。Further, in the step 1), the forward osmosis drawing liquid adopts inorganic salt system drawing liquid, and the initial concentration of the third-level drawing liquid is 2M, which can ensure that the concentration of the drawing liquid reaches 0.5M when entering the first-level forward osmosis system, which is harmful to black and odorous water. Still has a good concentration effect.
进一步的,所述步骤1)中,一级稀释汲取液送入反渗透单元浓缩至2M后返回三级正渗透系统。Further, in the step 1), the first-stage diluted draw solution is sent to the reverse osmosis unit to be concentrated to 2M and then returned to the third-stage forward osmosis system.
进一步的,所述步骤2)中,以PAC为混凝剂,混合反应阶段采用空气搅拌混合的方式,促进Fe2+、Mn2+的氧化沉淀。Further, in the step 2), PAC is used as a coagulant, and air stirring is adopted in the mixing reaction stage to promote the oxidation precipitation of Fe 2+ and Mn 2+ .
进一步的,所述步骤3)中,缺氧池中装填悬浮填料,挂膜后利用缺氧生物膜对黑臭水浓缩液进行缺氧水解,缺氧池水力停留时间为2~4小时。Further, in the step 3), the anoxic tank is filled with suspended fillers, and the anoxic biofilm is used to perform anoxic hydrolysis of the black and odorous water concentrate after the film is formed, and the hydraulic retention time of the anoxic tank is 2 to 4 hours.
本发明具有以下积极的效果:The present invention has the following positive effects:
本方法是一种用于黑臭水的物化-生化组合应急处理方法,其优点是:黑臭水经大幅浓缩、减容后再进行后续处理,可有效缩减处理量、提高效率;采用梯级浓缩的方式,单级通量低,膜污染程度轻,多次循环后,通量保持在较稳定的水平,可实现连续操作;汲取液通过正渗透、反渗透循环稀释、浓缩,避免二次污染;黑臭水浓缩处理后,Fe、Mn等至黑因子通过混凝去除,有机污染物经缺氧水解后最终进入污水厂,避免了曝气、原位投加混凝剂等常规方法污染物依然停留在水体中的缺点。The method is a physicochemical-biochemical combined emergency treatment method for black and odorous water. The single-stage flux is low and the degree of membrane fouling is light. After multiple cycles, the flux is kept at a relatively stable level, and continuous operation can be realized; ; After the black and odorous water is concentrated, Fe, Mn and other black factors are removed by coagulation, and organic pollutants are finally entered into the sewage treatment plant after anoxic hydrolysis, avoiding conventional methods such as aeration and in-situ dosing of coagulants. The disadvantage of still staying in a body of water.
附图说明Description of drawings
图1是本发明黑臭水正渗透-混凝-缺氧水解组合应急处理方法的流程图。Fig. 1 is the flow chart of the combined emergency treatment method of black and odorous water by forward osmosis-coagulation-anoxic hydrolysis of the present invention.
图2是实施例1黑臭水第三级正渗透通量随周期的变化规律。Fig. 2 is the variation law of the third-stage forward osmosis flux of black and odorous water in Example 1 with the period.
具体实施方式Detailed ways
以下实施例进一步说明本发明的内容,但不应理解为对本发明的限制。在不背离本发明精神和实质的情况下,对本发明方法、步骤或条件所作的修改或替换,均属于本发明的范围。The following examples further illustrate the content of the present invention, but should not be construed as limiting the present invention. Modifications or substitutions made to the methods, steps or conditions of the present invention without departing from the spirit and essence of the present invention all belong to the scope of the present invention.
结合图1,本发明的黑臭水正渗透-混凝-缺氧水解组合应急处理方法,过程如下:1, the black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method of the present invention, the process is as follows:
黑臭水首先通过梯级正渗透进行三级浓缩处理,一级、二级正渗透浓缩倍数均采用2倍,三级正渗透浓缩倍数采用3倍,正渗透汲取液采用无机盐系汲取液,三级汲取液初始浓度为2M,三级汲取液渗透稀释后送入二级正渗透继续汲取操作,最后送入一级正渗透进行黑臭水浓缩,汲取液进入一级正渗透系统时浓度为0.5M,对黑臭水依然具有良好的浓缩效果。黑臭水经梯级浓缩后减容12倍,主要污染物浓度提高10倍左右。一级稀释汲取液再送入反渗透单元浓缩至2M后返回三级正渗透系统。The black and odorous water is firstly subjected to three-stage concentration treatment through stepped forward osmosis. The concentration ratio of first-stage and second-stage forward osmosis is 2 times, and the concentration ratio of third-stage forward osmosis is 3 times. The initial concentration of the first-level drawing liquid is 2M, the third-level drawing liquid is osmotically diluted and sent to the second-level forward osmosis to continue the drawing operation, and finally sent to the first-level forward osmosis for black and odorous water concentration. The concentration of the drawing liquid entering the first-level forward osmosis system is 0.5 M, still has a good concentration effect on black and odorous water. The black and odorous water is reduced by 12 times after the cascade concentration, and the concentration of the main pollutants is increased by about 10 times. The first-stage diluted drawing liquid is sent to the reverse osmosis unit to be concentrated to 2M and then returned to the third-stage forward osmosis system.
黑臭水浓缩液进入混凝沉淀处理装置,以PAC为混凝剂,混合反应阶段采用空气搅拌混合的方式,去除铁、锰及水中悬浮物、胶体物质;黑臭水浓缩液再送入生物膜缺氧池,缺氧池中装填悬浮填料,挂膜后利用缺氧生物膜对黑臭水浓缩液进行缺氧水解,缺氧池水力停留时间为2~4小时,经缺氧水解的浓缩水可生化性提高,有机负荷降低,出水最终排入市政污水管网送污水厂进行集中处理。The black and odorous water concentrate enters the coagulation and sedimentation treatment device, and PAC is used as a coagulant. In the mixing reaction stage, air stirring and mixing are used to remove iron, manganese, suspended solids and colloidal substances in water; the black and odorous water concentrate is sent to the biofilm. Anoxic tank, the anoxic tank is filled with suspended fillers, and the anoxic biofilm is used to perform anoxic hydrolysis of the black and odorous water concentrate after filming. The biodegradability is improved, the organic load is reduced, and the effluent is finally discharged into the municipal sewage pipe network and sent to the sewage treatment plant for centralized treatment.
实施例1Example 1
试验期间采用江苏省南京市某黑臭水体为处理对象,黑臭水首先通过梯级正渗透(FO)进行三级浓缩处理,进水COD(化学需氧量)浓度介于50.4-60mg/L范围内,NH4 +-N(氨态氮)为2.0-4.2mg/L,TP(总磷,污水中常测的一种污染物)为0.26-0.29mg/L。一级、二级正渗透浓缩倍数均采用2倍,三级正渗透浓缩倍数采用3倍,正渗透汲取液为氯化钠溶液(氯化钠产地:国药集团化学试剂有限公司),三级汲取液初始浓度为2M,三级汲取液渗透稀释后送入二级正渗透继续汲取操作,一级稀释汲取液送入反渗透单元浓缩至2M后再返回三级正渗透系统。经三级FO浓缩后黑臭水COD浓度范围提高至480-550mg/L,废水可生化性偏低(B/C比在0.22-0.28范围内)。During the test, a black and odorous water body in Nanjing City, Jiangsu Province was used as the treatment object. The black and odorous water was first subjected to three-stage concentration treatment through stepped forward osmosis (FO), and the influent COD (chemical oxygen demand) concentration was in the range of 50.4-60mg/L Inside, NH 4 + -N (ammonia nitrogen) is 2.0-4.2mg/L, and TP (total phosphorus, a pollutant commonly measured in sewage) is 0.26-0.29mg/L. The forward osmosis concentration ratio of the first and second stage is 2 times, and the forward osmosis concentration ratio of the third stage is 3 times. The forward osmosis drawing solution is sodium chloride solution (sodium chloride origin: Sinopharm Chemical Reagent Co., Ltd.) The initial concentration of the liquid is 2M. After osmosis and dilution, the third-level drawing liquid is sent to the second-level forward osmosis to continue the drawing operation. The first-level diluted drawing liquid is sent to the reverse osmosis unit to be concentrated to 2M and then returned to the third-level forward osmosis system. After three-stage FO concentration, the COD concentration range of black and odorous water is increased to 480-550mg/L, and the biodegradability of wastewater is low (B/C ratio is in the range of 0.22-0.28).
黑臭水浓缩液进入混凝沉淀处理装置,本实施例以PAC(聚合氧化铝)为混凝剂,混合反应阶段采用空气搅拌混合的方式,以去除铁、锰及水中悬浮物、胶体物质。The black and odorous water concentrate enters the coagulation and sedimentation treatment device. In this example, PAC (polymeric alumina) is used as the coagulant, and the mixing reaction stage adopts air stirring and mixing to remove iron, manganese and suspended solids and colloidal substances in water.
黑臭水浓缩液再送入生物膜缺氧池,缺氧池中装填球型悬浮填料(Φ100mm,产地:宜兴景天环保科技有限公司),挂膜后利用缺氧生物膜对黑臭水浓缩液进行缺氧水解,缺氧池水力停留时间为2~4小时。The black and odorous water concentrate is then sent to the biofilm anoxic tank, and the anoxic tank is filled with spherical suspension filler (Φ100mm, origin: Yixing Jingtian Environmental Protection Technology Co., Ltd.), and the anoxic biofilm is used to treat the black and odorous water concentrate after hanging the film. For anoxic hydrolysis, the hydraulic retention time of the anoxic pool is 2 to 4 hours.
黑臭水浓缩液经混凝沉淀-缺氧水解后,COD降至390-440mg/L,B/C比提高至0.35左右,浓缩水可生化性提高,有机负荷降低,废水其他主要指标达污水综合排放标准(GB8978-1996)三级排放标准后可纳入市政污水管网送污水处理厂作进一步处理。After coagulation sedimentation and anoxic hydrolysis of the black and odorous water concentrate, the COD is reduced to 390-440mg/L, the B/C ratio is increased to about 0.35, the biodegradability of the concentrated water is improved, the organic load is reduced, and other major indicators of waste water reach sewage. The comprehensive discharge standard (GB8978-1996) can be incorporated into the municipal sewage pipe network and sent to the sewage treatment plant for further treatment after the three-level discharge standard.
对本实施例正渗透过程的通量监测表明,正渗透处理黑臭水膜污染程度轻,每个浓缩周期仅采用简单的物理清洗方法,从图2可以看出,新膜第一个运行周期通量最高,从第二周期开始通量有一定程度的下降,但此后随着运行时间的延长可保持在较稳定的水平。The flux monitoring of the forward osmosis process in this example shows that the black and odorous water membrane of the forward osmosis treatment has a low degree of pollution, and only a simple physical cleaning method is used in each concentration cycle. It can be seen from Figure 2 that the first operating cycle of the new membrane The flux was the highest, and the flux decreased to a certain extent from the second cycle, but after that, it could be maintained at a relatively stable level with the extension of the running time.
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CN108706839A (en) * | 2018-07-31 | 2018-10-26 | 山东默锐环境产业股份有限公司 | A kind of chemical industrial park comprehensive wastewater treatment system with high salt |
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