CN106977007A - The system and method for bi-membrane method advanced treating brown alga chemical industry waste Ca water - Google Patents
The system and method for bi-membrane method advanced treating brown alga chemical industry waste Ca water Download PDFInfo
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Abstract
本发明公开了双膜法深度处理褐藻化工废钙水的系统和方法,该系统为:双膜法深度处理褐藻化工废钙水的系统,褐藻化工废钙水管道8依次与混凝‑气浮处理池1、陶瓷膜组件2、活性炭罐3和反渗透膜组件4连接,反渗透膜组件4连接有生产用水管9;陶瓷膜组件2通过管道与沉降槽6连接,沉降槽6通过管道依次与氧化反应器7和所述混凝‑气浮处理池1连接。本发明用陶瓷膜组件作为处理废钙水的预处理,简化了工艺处理步骤,陶瓷膜组件占地面积少,处理实际污水效能高。利用陶瓷超滤膜系统预处理后,可显著降低反渗透膜的污染,降低了前处理过程成本,易于工艺放大。
The invention discloses a system and method for advanced treatment of waste calcium water from brown algae chemical industry by double-membrane method. The system is: a system for advanced treatment of waste calcium water from brown algae chemical industry by double-membrane method. The treatment tank 1, the ceramic membrane module 2, the activated carbon tank 3 and the reverse osmosis membrane module 4 are connected, and the reverse osmosis membrane module 4 is connected with the production water pipe 9; the ceramic membrane module 2 is connected with the settling tank 6 through the pipeline, and the settling tank 6 is sequentially passed through the pipeline It is connected with the oxidation reactor 7 and the coagulation-air flotation treatment tank 1. The present invention uses ceramic membrane modules as pretreatment for treating waste calcium water, simplifies process steps, occupies less floor space, and has high efficiency in treating actual sewage. After pretreatment with the ceramic ultrafiltration membrane system, the pollution of the reverse osmosis membrane can be significantly reduced, the cost of the pretreatment process is reduced, and the process is easy to scale up.
Description
技术领域technical field
本发明涉及海藻工业生产污水处理的领域,尤其是对海藻酸钠产品生产工艺中产生废钙水的处理。The invention relates to the field of sewage treatment of seaweed industrial production, in particular to the treatment of waste calcium water produced in the production process of sodium alginate products.
背景技术Background technique
海藻加工产品主要有红藻胶质制品和褐藻化工产品两类。我国褐藻胶产品年生产能力约为3.5万吨,占世界总生产能力的60%,是我国海藻加工行业中的支柱产品,已经广泛应用于印染、医药、食品、日用品等领域。生产1吨褐藻胶将消耗淡水1000吨,产生的废钙水占全部废水的70%以上。上述污水经过处理再回用将能够有效降低企业生产成本、节约淡水资源,产生巨大的经济、社会和环境效益。Seaweed processing products mainly include red algae gelatinous products and brown algae chemical products. my country's annual production capacity of alginate products is about 35,000 tons, accounting for 60% of the world's total production capacity. It is a pillar product in my country's seaweed processing industry and has been widely used in printing and dyeing, medicine, food, daily necessities and other fields. The production of 1 ton of alginate will consume 1,000 tons of fresh water, and the waste calcium water produced will account for more than 70% of all wastewater. The reuse of the above-mentioned sewage after treatment will effectively reduce the production cost of enterprises, save fresh water resources, and generate huge economic, social and environmental benefits.
钙废水含有大量的Ca2+、K+、ClO-、SO42-、Cl-以及海藻胶、多糖、蛋白质以及海带淀粉等有机污染物。由于废水量大,成分复杂,传统的水处理技术(例如气浮)只能一定程度降低废水COD的含量实现达标排放。随着水资源的日趋紧张和我国越来越严格的环境保护要求,实现对废钙水深度处理回用已经势在必行。CN101074140A中国发明专利“褐藻胶生产废水的处理及循环回用零排放的工艺方法”,说明了本发明将褐藻胶生产产生的废钙水进行氧化,脱钙处理,生物过滤氧化处理,气浮处理,絮凝、沉淀处理;两者混合后的综合水经臭氧循环氧化处理处理,再经过滤生物氧化处理后,最后经过反渗透装置深度处理。基于多步预处理加反渗透深度处理技术实现了废钙水零排放处理。但是该发明前处理步骤复杂,设备费用和占地面积规模过大,并且加入多种化学试剂不仅增加了处理成本而且为接下来的处理工艺造成了影响。2012年公开的CN102745841A中国发明专利“一种褐藻化工废钙水新型循环回用工艺”,说明了一种化学沉淀、电渗析及离子交换结合工艺处理废钙水技术;该发明中电渗析工艺能耗过高,再生生成本高昂,而且产生大量再生废液,处理实际污水成本代价太大,不具有实用价值。Calcium wastewater contains a large amount of Ca 2+ , K + , ClO - , SO4 2- , Cl - and organic pollutants such as alginate, polysaccharide, protein and kelp starch. Due to the large amount of wastewater and complex components, traditional water treatment technologies (such as air flotation) can only reduce the COD content of wastewater to a certain extent to achieve discharge standards. With the increasingly tense water resources and my country's increasingly stringent environmental protection requirements, it is imperative to realize the advanced treatment and reuse of waste calcium water. CN101074140A Chinese invention patent "treatment of alginate production wastewater and recycling zero-emission process", which illustrates that the present invention oxidizes the waste calcium water produced by alginate production, decalcifies treatment, biological filtration oxidation treatment, and air flotation treatment , flocculation and sedimentation treatment; the comprehensive water after the mixture of the two is treated by ozone cycle oxidation treatment, and then filtered and biologically oxidized, and finally advanced treatment by reverse osmosis device. Based on multi-step pretreatment plus reverse osmosis advanced treatment technology, zero discharge treatment of waste calcium water is realized. However, the pretreatment steps of the invention are complicated, the equipment cost and floor area are too large, and the addition of various chemical reagents not only increases the treatment cost but also affects the subsequent treatment process. The Chinese invention patent CN102745841A published in 2012, "A New Recycling Process for Brown Algae Chemical Waste Calcium Water", describes a combined process of chemical precipitation, electrodialysis and ion exchange to treat waste calcium water; the electrodialysis process in this invention can The consumption is too high, the cost of regeneration is high, and a large amount of regeneration waste liquid is produced, the cost of treating actual sewage is too high, and it has no practical value.
总结上述工艺发明可以看出,大多数的公开发明仍专注于通过化学法处理废钙水实现回用的目的。但是上述技术仍需要使用大量化学药剂,同时废钙水经处理回用后仍将产生大量高盐废水,后期废水处理更加困难。Summarizing the above process inventions, it can be seen that most of the disclosed inventions still focus on the purpose of recycling calcium waste water through chemical treatment. However, the above-mentioned technology still needs to use a large amount of chemical agents, and at the same time, the waste calcium water will still produce a large amount of high-salt wastewater after treatment and reuse, and the later wastewater treatment is more difficult.
目前使用陶瓷膜组件处理褐藻化工废钙水的方法未见有报道。At present, there is no report on the method of using ceramic membrane modules to treat brown algae chemical waste calcium water.
发明内容Contents of the invention
本发明的目的是克服现有技术的不足,提供一种双膜法深度处理褐藻化工废钙水的系统。The purpose of the present invention is to overcome the deficiencies of the prior art and provide a system for the advanced treatment of brown algae chemical waste calcium water by double-membrane method.
本发明的第二个目的是提供一种双膜法深度处理褐藻化工废钙水的方法。The second object of the present invention is to provide a double-membrane method for advanced treatment of brown algae chemical waste calcium water.
本发明的技术方案概述如下:Technical scheme of the present invention is summarized as follows:
双膜法深度处理褐藻化工废钙水的系统,褐藻化工废钙水管道8依次与混凝-气浮处理池1、陶瓷膜组件2、活性炭罐3和反渗透膜组件4连接,反渗透膜组件4连接有生产用水管9;陶瓷膜组件2通过管道与沉降槽6连接,沉降槽6通过管道依次与氧化反应器7和所述混凝-气浮处理池1连接。A system for the advanced treatment of brown algae chemical waste calcium water by double membrane method. Brown algae chemical waste calcium water pipeline 8 is sequentially connected with coagulation-air flotation treatment tank 1, ceramic membrane module 2, activated carbon tank 3 and reverse osmosis membrane module 4. The reverse osmosis membrane The module 4 is connected with a production water pipe 9; the ceramic membrane module 2 is connected with the settling tank 6 through the pipeline, and the settling tank 6 is connected with the oxidation reactor 7 and the coagulation-air flotation treatment tank 1 in turn through the pipeline.
陶瓷膜组件2为表面具有亲水性的陶瓷膜组件,所述陶瓷膜组件2为平板陶瓷膜组件或管式陶瓷膜组件,所述陶瓷膜的平均孔径10nm-200nm。The ceramic membrane module 2 is a ceramic membrane module with a hydrophilic surface. The ceramic membrane module 2 is a flat ceramic membrane module or a tubular ceramic membrane module. The average pore diameter of the ceramic membrane is 10nm-200nm.
反渗透膜组件4为中空反渗透膜组件、管式反渗透膜组件、平板反渗透膜组件、卷式反渗透膜组件或碟片式反渗透膜组件。The reverse osmosis membrane module 4 is a hollow reverse osmosis membrane module, a tube-type reverse osmosis membrane module, a flat-plate reverse osmosis membrane module, a roll-type reverse osmosis membrane module or a disk-type reverse osmosis membrane module.
双膜法深度处理褐藻化工废钙水的方法,包括如下步骤:The method for advanced treatment of brown algae chemical waste calcium water by double-membrane method comprises the following steps:
(1)使用权利要求1的双膜法深度处理褐藻化工废钙水的系统;(1) use the double-membrane method advanced treatment system of brown algae chemical waste calcium water of claim 1;
(2)将褐藻化工废钙水通过褐藻化工废钙水管道8输入混凝-气浮处理池1中脱除褐藻胶后输入陶瓷膜组件2,在运行压力为0.1-0.4MPa的条件下分离得到滤液1和浓水,滤液1通入活性炭罐3过滤后通入反渗透膜组件4,在运行压力为0.6-1.5MPa的条件下过滤,再经生产用水管9输出生产用水;所述浓水通过管道输入沉降槽6进行沉降后,上清液输入氧化反应器7,用次氯酸钠进行氧化,经氧化反应后回流至混凝-气浮处理池1。反渗透浓水可以经过热法浓缩达到零排放处理。(2) Put the brown algae chemical waste calcium water into the coagulation-air flotation treatment tank 1 through the brown algae chemical waste calcium water pipeline 8 to remove the alginate and then into the ceramic membrane module 2, and separate it under the condition of operating pressure of 0.1-0.4MPa Obtain filtrate 1 and concentrated water, filtrate 1 is passed into activated carbon tank 3 for filtration and then passed into reverse osmosis membrane module 4, filtered under the condition of operating pressure of 0.6-1.5MPa, and then output production water through production water pipe 9; After the water is input into the settling tank 6 through the pipeline for sedimentation, the supernatant is input into the oxidation reactor 7, oxidized with sodium hypochlorite, and returned to the coagulation-air flotation treatment tank 1 after the oxidation reaction. Reverse osmosis concentrated water can be concentrated by thermal method to achieve zero discharge treatment.
本发明的优点:Advantages of the present invention:
本发明用陶瓷膜组件作为处理废钙水的预处理,简化了工艺处理步骤,陶瓷膜组件占地面积少,处理实际污水效能高。利用陶瓷超滤膜系统预处理后,可显著降低反渗透膜的污染,简化了预处理工艺,降低了前处理过程成本,易于工艺放大。The present invention uses ceramic membrane modules as pretreatment for treating waste calcium water, simplifies process steps, occupies less floor space, and has high efficiency in treating actual sewage. After pretreatment with the ceramic ultrafiltration membrane system, the pollution of the reverse osmosis membrane can be significantly reduced, the pretreatment process is simplified, the cost of the pretreatment process is reduced, and the process is easy to scale up.
附图说明Description of drawings
图1为双膜法深度处理褐藻化工废钙水的系统的示意图。Figure 1 is a schematic diagram of a system for advanced treatment of brown algae chemical waste calcium water by double-membrane method.
具体实施方式detailed description
下面结合附图和具体实施例对本发明作进一步的说明。The present invention will be further described below in conjunction with the accompanying drawings and specific embodiments.
双膜法深度处理褐藻化工废钙水的系统,见图1,褐藻化工废钙水管道8依次与混凝-气浮处理池1、陶瓷膜组件2、活性炭罐3和反渗透膜组件4,反渗透膜组件4连接有生产用水管9;陶瓷膜组件2通过管道与沉降槽6连接,沉降槽6通过管道依次与氧化反应器7和所述混凝-气浮处理池1连接。The system for the advanced treatment of brown algae chemical waste calcium water by double-membrane method is shown in Figure 1. The brown algae chemical waste calcium water pipeline 8 is sequentially connected with the coagulation-air flotation treatment tank 1, ceramic membrane module 2, activated carbon tank 3 and reverse osmosis membrane module 4, The reverse osmosis membrane module 4 is connected to the production water pipe 9; the ceramic membrane module 2 is connected to the settling tank 6 through the pipeline, and the settling tank 6 is connected to the oxidation reactor 7 and the coagulation-air flotation treatment tank 1 in turn through the pipeline.
还可以在反渗透膜组件4和生产用水管9之间连接一高压反渗透膜组件。A high-pressure reverse osmosis membrane module can also be connected between the reverse osmosis membrane module 4 and the production water pipe 9 .
陶瓷膜组件2为表面具有亲水性的陶瓷膜组件,所述陶瓷膜组件2为平板陶瓷膜组件或管式陶瓷膜组件,所述陶瓷膜的平均孔径10nm-200nm。The ceramic membrane module 2 is a ceramic membrane module with a hydrophilic surface. The ceramic membrane module 2 is a flat ceramic membrane module or a tubular ceramic membrane module. The average pore diameter of the ceramic membrane is 10nm-200nm.
反渗透膜组件4为中空反渗透膜组件、管式反渗透膜组件、平板反渗透膜组件、卷式反渗透膜组件或碟管式反渗透膜组件。The reverse osmosis membrane module 4 is a hollow reverse osmosis membrane module, a tubular reverse osmosis membrane module, a flat reverse osmosis membrane module, a roll type reverse osmosis membrane module or a disc tube type reverse osmosis membrane module.
实施例1Example 1
双膜法深度处理褐藻化工废钙水的方法,包括如下步骤:The method for advanced treatment of brown algae chemical waste calcium water by double-membrane method comprises the following steps:
(1)使用双膜法深度处理褐藻化工废钙水的系统;其中的陶瓷膜组件2为表面具有亲水性的平板陶瓷膜组件,陶瓷膜的平均孔径100nm;反渗透膜组件4为中空反渗透膜组件;(1) A system for advanced treatment of brown algae chemical waste calcium water using a double-membrane method; the ceramic membrane module 2 is a flat ceramic membrane module with a hydrophilic surface, and the average pore size of the ceramic membrane is 100nm; the reverse osmosis membrane module 4 is a hollow reverse osmosis membrane module. Permeable membrane components;
(2)将褐藻化工废钙水通过褐藻化工废钙水管道8输入混凝-气浮处理池1中脱除褐藻胶后输入陶瓷膜组件2,在运行压力为0.2MPa的条件下分离得到滤液1和浓水,滤液1通入活性炭罐3过滤后通入反渗透膜组件4,在运行压力为1.0MPa的条件下过滤,再经生产用水管9输出生产用水;所述浓水通过管道输入沉降槽6进行沉降后,上清液输入氧化反应器7,用次氯酸钠进行氧化,经氧化反应后回流至混凝-气浮处理池1。见表1。(2) The brown algae chemical waste calcium water is input into the coagulation-air flotation treatment tank 1 through the brown algae chemical waste calcium water pipeline 8 to remove alginate, and then input into the ceramic membrane module 2, and the filtrate is obtained by separating under the condition of operating pressure of 0.2 MPa 1 and concentrated water, the filtrate 1 is passed into the activated carbon tank 3 for filtration and then passed into the reverse osmosis membrane module 4, filtered under the condition of operating pressure of 1.0MPa, and then output the production water through the production water pipe 9; the concentrated water is input through the pipeline After settling in the settling tank 6, the supernatant is input into the oxidation reactor 7, oxidized with sodium hypochlorite, and returned to the coagulation-air flotation treatment tank 1 after the oxidation reaction. See Table 1.
表1实施例1处理褐藻化工废钙水水质数据:单位为mg/LTable 1 Example 1 Treatment of Brown Algae Chemical Waste Calcium Water Water Quality Data: Unit is mg/L
实施例2Example 2
双膜法深度处理褐藻化工废钙水的方法,包括如下步骤:The method for advanced treatment of brown algae chemical waste calcium water by double-membrane method comprises the following steps:
(1)使用双膜法深度处理褐藻化工废钙水的系统;其中的陶瓷膜组件2为表面具有亲水性的管式陶瓷膜组件,陶瓷膜的平均孔径10nm;反渗透膜组件4为管式反渗透膜组件;(1) A system for advanced treatment of waste calcium water from brown algae chemical industry using a double-membrane method; the ceramic membrane module 2 is a tubular ceramic membrane module with a hydrophilic surface, and the average pore size of the ceramic membrane is 10nm; the reverse osmosis membrane module 4 is a tubular ceramic membrane module. reverse osmosis membrane module;
(2)将褐藻化工废钙水通过褐藻化工废钙水管道8输入混凝-气浮处理池1中脱除褐藻胶后输入陶瓷膜组件2,在运行压力为0.1MPa的条件下分离得到滤液1和浓水,滤液1通入活性炭罐3过滤后通入反渗透膜组件4,在运行压力为0.6MPa的条件下过滤,再经生产用水管9输出生产用水;所述浓水通过管道输入沉降槽6进行沉降后,上清液输入氧化反应器7,用次氯酸钠进行氧化,经氧化反应后回流至混凝-气浮处理池1。(2) The brown algae chemical waste calcium water is input into the coagulation-air flotation treatment tank 1 through the brown algae chemical waste calcium water pipeline 8 to remove the alginate, and then input into the ceramic membrane module 2, and the filtrate is obtained by separating under the condition of an operating pressure of 0.1 MPa 1 and concentrated water, the filtrate 1 is passed into the activated carbon tank 3 for filtration and then passed into the reverse osmosis membrane module 4, filtered under the condition of operating pressure of 0.6MPa, and then the production water is output through the production water pipe 9; the concentrated water is input through the pipeline After settling in the settling tank 6, the supernatant is input into the oxidation reactor 7, oxidized with sodium hypochlorite, and returned to the coagulation-air flotation treatment tank 1 after the oxidation reaction.
实施例3Example 3
双膜法深度处理褐藻化工废钙水的方法,包括如下步骤:The method for advanced treatment of brown algae chemical waste calcium water by double-membrane method comprises the following steps:
(1)使用双膜法深度处理褐藻化工废钙水的系统;其中的陶瓷膜组件2为表面具有亲水性的管式陶瓷膜组件,陶瓷膜的平均孔径200nm;反渗透膜组件4为平板反渗透膜组件;(1) A system for advanced treatment of waste calcium water from brown algae chemical industry using a double-membrane method; the ceramic membrane module 2 is a tubular ceramic membrane module with a hydrophilic surface, and the average pore size of the ceramic membrane is 200nm; the reverse osmosis membrane module 4 is a flat plate reverse osmosis membrane components;
(2)将褐藻化工废钙水通过褐藻化工废钙水管道8输入混凝-气浮处理池1中脱除褐藻胶后输入陶瓷膜组件2,在运行压力为0.4MPa的条件下分离得到滤液1和浓水,滤液1通入活性炭罐3过滤后通入反渗透膜组件4,在运行压力为1.5MPa的条件下过滤,再经生产用水管9输出生产用水;所述浓水通过管道输入沉降槽6进行沉降后,上清液输入氧化反应器7,用次氯酸钠进行氧化,经氧化反应后回流至混凝-气浮处理池1。(2) The brown algae chemical waste calcium water is input into the coagulation-air flotation treatment tank 1 through the brown algae chemical waste calcium water pipeline 8 to remove the alginate, and then input into the ceramic membrane module 2, and the filtrate is obtained by separating under the condition of an operating pressure of 0.4MPa 1 and concentrated water, the filtrate 1 is passed into the activated carbon tank 3 for filtration and then passed into the reverse osmosis membrane module 4, filtered under the condition of operating pressure of 1.5MPa, and then the production water is output through the production water pipe 9; the concentrated water is input through the pipeline After settling in the settling tank 6, the supernatant is input into the oxidation reactor 7, oxidized with sodium hypochlorite, and returned to the coagulation-air flotation treatment tank 1 after the oxidation reaction.
还可以用卷式反渗透膜组件或碟管式反渗透膜组件替代本实施例中的平板反渗透膜组件作为反渗透膜组件4,其它同本实施例对褐藻化工废钙水进行处理。The flat reverse osmosis membrane module in this embodiment can also be replaced by a roll type reverse osmosis membrane module or a disc tube type reverse osmosis membrane module as the reverse osmosis membrane module 4, and the other is the same as in this embodiment for the treatment of brown algae chemical waste calcium water.
本发明使用次氯酸钠氧化经陶瓷膜组件分离再经沉淀后的污水,不会引入新的杂质粒子,成本低廉,和其他的一些氧化试剂比如芬顿相比较不会产生大量污泥,水质颜色澄清。The present invention uses sodium hypochlorite to oxidize the sewage separated by ceramic membrane modules and then precipitated, without introducing new impurity particles, low in cost, and does not produce a large amount of sludge compared with other oxidizing reagents such as Fenton, and the water quality is clear in color.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107555660A (en) * | 2017-09-30 | 2018-01-09 | 三达膜科技(厦门)有限公司 | A kind of drink water purifying method |
| CN119430585A (en) * | 2025-01-06 | 2025-02-14 | 金科环境股份有限公司 | A treatment system and method for sodium alginate production wastewater |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690003A (en) * | 2012-06-19 | 2012-09-26 | 江苏久吾高科技股份有限公司 | Device and method for performing advanced treatment on citric acid waste water through dual membrane process |
| WO2014151354A1 (en) * | 2013-03-14 | 2014-09-25 | Veolia Water Solutions & Technologies North America, Inc. | Process for water treatment prior to reverse osmosis |
| CN205803169U (en) * | 2016-06-02 | 2016-12-14 | 中国水产科学研究院黄海水产研究所 | A kind of algin production waste water recycling system |
| CN106315932A (en) * | 2016-08-24 | 2017-01-11 | 厦门世达膜科技有限公司 | Method for disposing wastewater from oil field |
| CN106396165A (en) * | 2016-06-30 | 2017-02-15 | 无锡龙盈环保科技有限公司 | A processing process and a processing device for turtle cultivation waste water |
-
2017
- 2017-03-29 CN CN201710197228.8A patent/CN106977007A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102690003A (en) * | 2012-06-19 | 2012-09-26 | 江苏久吾高科技股份有限公司 | Device and method for performing advanced treatment on citric acid waste water through dual membrane process |
| WO2014151354A1 (en) * | 2013-03-14 | 2014-09-25 | Veolia Water Solutions & Technologies North America, Inc. | Process for water treatment prior to reverse osmosis |
| CN205803169U (en) * | 2016-06-02 | 2016-12-14 | 中国水产科学研究院黄海水产研究所 | A kind of algin production waste water recycling system |
| CN106396165A (en) * | 2016-06-30 | 2017-02-15 | 无锡龙盈环保科技有限公司 | A processing process and a processing device for turtle cultivation waste water |
| CN106315932A (en) * | 2016-08-24 | 2017-01-11 | 厦门世达膜科技有限公司 | Method for disposing wastewater from oil field |
Non-Patent Citations (1)
| Title |
|---|
| 刘硕等: "《自然地理与资源环境专业实验教程》", 31 July 2016, 哈尔滨工程大学出版社 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107555660A (en) * | 2017-09-30 | 2018-01-09 | 三达膜科技(厦门)有限公司 | A kind of drink water purifying method |
| CN119430585A (en) * | 2025-01-06 | 2025-02-14 | 金科环境股份有限公司 | A treatment system and method for sodium alginate production wastewater |
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