[go: up one dir, main page]

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 PDF

Info

Publication number
CN111892238A
CN111892238A CN202010662414.6A CN202010662414A CN111892238A CN 111892238 A CN111892238 A CN 111892238A CN 202010662414 A CN202010662414 A CN 202010662414A CN 111892238 A CN111892238 A CN 111892238A
Authority
CN
China
Prior art keywords
black
forward osmosis
odorous water
concentration
water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202010662414.6A
Other languages
Chinese (zh)
Other versions
CN111892238B (en
Inventor
张勇
何佳颖
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nanjing Normal University
Original Assignee
Nanjing Normal University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nanjing Normal University filed Critical Nanjing Normal University
Priority to CN202010662414.6A priority Critical patent/CN111892238B/en
Publication of CN111892238A publication Critical patent/CN111892238A/en
Application granted granted Critical
Publication of CN111892238B publication Critical patent/CN111892238B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/445Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by forward osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
    • C02F1/74Treatment of water, waste water, or sewage by oxidation with air
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/203Iron or iron compound
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • C02F2101/206Manganese or manganese compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/30Organic compounds
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/28Anaerobic digestion processes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

The invention discloses a black odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method, wherein black odorous water is subjected to three-stage concentration treatment by step forward osmosis, and the step concentration ensures that the single-stage flux is low, the membrane pollution degree is light, and the continuous operation can be realized; the drawing liquid diluted in the forward osmosis process is subjected to re-concentration and recycling by adopting reverse osmosis, so that secondary pollution can be avoided; the concentrated black and odorous water volume is greatly reduced, the concentrations of organic matters, iron, manganese and the like are obviously improved, the treatment capacity is effectively reduced, and the efficiency is improved; iron, manganese, suspended matters and colloidal substances in water are removed through coagulating sedimentation in sequence, anoxic hydrolysis is performed to improve biodegradability of concentrated water, and effluent finally enters a sewage plant, so that the defect that pollutants stay in a water body in conventional methods such as aeration, in-situ coagulant adding and the like is overcome.

Description

一种黑臭水正渗透-混凝-缺氧水解组合应急处理方法A combined emergency treatment method for black and odorous water with forward osmosis-coagulation-anoxic hydrolysis

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.

Claims (5)

1.一种黑臭水正渗透-混凝-缺氧水解组合应急处理方法,其特征在于,包括如下步骤:1. a black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method, is characterized in that, comprises the 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. 2.根据权利要求1所述的黑臭水正渗透-混凝-缺氧水解组合应急处理方法,其特征在于,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。2. The combined emergency treatment method for black and odorous water according to claim 1, characterized in that, in the step 1), both the primary and secondary forward osmosis concentration ratios are 2 times , the three-stage forward osmosis concentration ratio is 3 times, and the black and odorous water is reduced by 12 times after the cascade concentration. 3.根据权利要求2所述的黑臭水正渗透-混凝-缺氧水解组合应急处理方法,其特征在于,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,一级稀释汲取液送入反渗透单元浓缩至2M。3. The method for combined emergency treatment of black and odorous water with forward osmosis-coagulation-anoxic hydrolysis according to claim 2, characterized in that, in the step 1), the forward osmosis drawing liquid adopts an inorganic salt system drawing liquid, and the three-stage The initial concentration of the draw solution is 2M, and the first-level diluted draw solution is sent to the reverse osmosis unit to be concentrated to 2M. 4.根据权利要求1所述的黑臭水正渗透-混凝-缺氧水解组合应急处理方法,其特征在于,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。4. The combined emergency treatment method for black and odorous water according to claim 1, characterized in that, in the step 2), PAC is used as a coagulant, and air agitation is adopted in the mixing reaction stage The mixing method promotes the oxidation precipitation of Fe 2+ and Mn 2+ . 5.根据权利要求1所述的黑臭水正渗透-混凝-缺氧水解组合应急处理方法,其特征在于,所述步骤3)中,缺氧池中装填悬浮填料,缺氧池水力停留时间为2~4小时。5. The combined emergency treatment method for black and odorous water according to claim 1, characterized in that, in the step 3), the anoxic tank is filled with suspended fillers, and the anoxic tank is hydraulically stopped. The time is 2~4 hours.
CN202010662414.6A 2020-07-10 2020-07-10 Black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method Active CN111892238B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202010662414.6A CN111892238B (en) 2020-07-10 2020-07-10 Black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202010662414.6A CN111892238B (en) 2020-07-10 2020-07-10 Black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method

Publications (2)

Publication Number Publication Date
CN111892238A true CN111892238A (en) 2020-11-06
CN111892238B CN111892238B (en) 2022-07-29

Family

ID=73192247

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202010662414.6A Active CN111892238B (en) 2020-07-10 2020-07-10 Black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method

Country Status (1)

Country Link
CN (1) CN111892238B (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106517669A (en) * 2016-12-16 2017-03-22 安徽师范大学 A/O forward osmosis treatment system and treatment process for black and odorous water
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
CN210206461U (en) * 2019-04-09 2020-03-31 中海石油炼化有限责任公司 Concentration device for low-hardness sodium chloride solution

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106517669A (en) * 2016-12-16 2017-03-22 安徽师范大学 A/O forward osmosis treatment system and treatment process for black and odorous water
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
CN210206461U (en) * 2019-04-09 2020-03-31 中海石油炼化有限责任公司 Concentration device for low-hardness sodium chloride solution

Also Published As

Publication number Publication date
CN111892238B (en) 2022-07-29

Similar Documents

Publication Publication Date Title
CN102040301B (en) Method for treating municipal waste leachate membrane concentrated solution
CN101759313B (en) Method for recycling high-salinity heavy metal-enriched waste water from vanadium extraction from stone coal
CN206476860U (en) A kind of oily waste water treatment reclamation set
CN102583884A (en) Method for treating mixed industrial sewage in industrial park
CN108455768A (en) It is a kind of using water reuse as the organic-inorganic polluted heavy metals production wastewater treatment method of core
CN103539319A (en) Garbage leachate treating device
CN102040309A (en) Combined treatment process for urban garbage percolate
CN103435158B (en) A kind of method strengthening MBR dephosphorization and lessening membrane fouling
CN102642995A (en) Method and system for physicochemical biological combined treatment of drilling wastewater of oil and gas field
CN212559887U (en) Water body deep purification system based on electrolytic denitrification and MBR
CN106282020B (en) A kind of method of the autotrophic denitrification micropopulation of orienting enriching different proportion
CN106007167B (en) The processing method of the pickling waste waters containing incretion interferent
CN202156978U (en) High salinity effluent treatment plant
CN106430590B (en) A high conductivity wastewater treatment method based on two-stage AO device
CN211664789U (en) Advanced treatment device for town sewage based on improved denitrification filter column
CN111892238B (en) Black and odorous water forward osmosis-coagulation-anoxic hydrolysis combined emergency treatment method
CN109231673B (en) A/O combined micro-electric field-Fe/C reinforced dephosphorization device and application thereof
CN106830582A (en) A kind of processing method of low biochemical cities and towns industrial park sewage
CN217459144U (en) Landfill leachate processing system based on electrocatalytic oxidation
CN2856037Y (en) Sewage reclaiming treatment unit
CN213623758U (en) Industrial wastewater treatment device
CN109626757A (en) A kind of method of light electrolysis-MBR coupling technique treatment of laboratory waste water
CN204588937U (en) A kind for the treatment of unit containing endocrine disrupter pickling waste waters
CN108409042A (en) It is a kind of using qualified discharge as the organic-inorganic heavy metal production wastewater treatment method of core
CN103253836B (en) A kind of percolate deep purifying treatment unit and method

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant