CN100335423C - Water purifying method for cultivation pond - Google Patents

Water purifying method for cultivation pond Download PDF

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CN100335423C
CN100335423C CNB2006100597501A CN200610059750A CN100335423C CN 100335423 C CN100335423 C CN 100335423C CN B2006100597501 A CNB2006100597501 A CN B2006100597501A CN 200610059750 A CN200610059750 A CN 200610059750A CN 100335423 C CN100335423 C CN 100335423C
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purification method
water body
body purification
cultivation
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CN1847167A (en
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岳平
唐文浩
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SOUTH-CHINA PROPICAL AGRICULTURAL UNIV
HAINAN RESEARCH ACADEMY OF ENVIRONMENTAL SCIENCES
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HAINAN RESEARCH ACADEMY OF ENVIRONMENTAL SCIENCES
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Abstract

The present invention discloses a water purifying method for a cultivation pond. The water purifying method comprises the following steps: cultivation waste water in the bottom layer at the center of a cultivation pond is pumped into a water bath by a water pump; suspended organic matters in the cultivation waste water are separated in the water bath; the cultivation waste water which is separated from the suspended organic matters is processed in a natural photochemical catalysis oxidation mode to return to the cultivation pond, and a water cycle is formed. The water purifying method of the present invention solves the problems that the administrative cost for water is high, and the environment is polluted existing in aquaculture, improves rationalization and biology conditions for cultivation water, and enhances the stability of cultivation hydroenvironment. The present invention is suitable for the water quality management of pond cultivation with sea and fresh water.

Description

一种养殖池塘的水体净化方法A kind of water body purification method of aquaculture pond

技术领域technical field

本发明涉及一种养殖池塘的水体净化方法,特别是一种养殖池塘的循环式水体净化方法。The invention relates to a water body purification method of a culture pond, in particular to a circulating water body purification method of a culture pond.

背景技术Background technique

针对规模化水产养殖水和排水中普遍存在的氮、磷、有机悬浮物及有害微生物等对养殖动物和水环境的不利影响,现有的解决措施主要是采取换水、投加化学氧化药剂或微生态菌剂、工业水净化、生态系统补偿等方法。换水措施是直接定期排放部分养殖废水后再补充部分新鲜的清洁水,以达到改善水体的理化和生物学条件的目的。换水的最大缺点是以牺牲环境为代价。定期投加化学氧化药剂的最大缺点是在氧化解毒的同时也破坏了养殖水体的生态平衡,运行成本高。定期投加微生态菌剂的最大缺点是易引起水体的理化和生物学指标产生大幅度波动,运行成本高。采用工业水净化处理方法的设备造价高,运行成本高。生态系统补偿方法主要原因存在占地面积大,运行管理难度较大等问题,在一定程度上影响了其应用。In view of the adverse effects of nitrogen, phosphorus, organic suspended solids and harmful microorganisms in the large-scale aquaculture water and drainage on the animals and the water environment, the existing solutions are mainly to change water, add chemical oxidants or Microecological agents, industrial water purification, ecosystem compensation and other methods. The measure of water change is to directly discharge part of the aquaculture wastewater regularly and then add some fresh clean water to achieve the purpose of improving the physical, chemical and biological conditions of the water body. The biggest downside to changing the water is at the expense of the environment. The biggest disadvantage of regular dosing of chemical oxidizing agents is that it destroys the ecological balance of the aquaculture water while oxidizing and detoxifying, and the operating cost is high. The biggest disadvantage of regular dosing of probiotics is that it is easy to cause large fluctuations in the physical, chemical and biological indicators of the water body, and the operating cost is high. The cost of equipment using industrial water purification treatment methods is high, and the operating cost is high. The main reasons for the ecological system compensation method are problems such as large land occupation and difficult operation and management, which affect its application to a certain extent.

发明内容Contents of the invention

本发明的目的是解决水产养殖中存在的水体管理成本高和污染环境的问题,改善养殖水体的理化和生物学条件以及增强养殖水环境的稳定性。The purpose of the invention is to solve the problems of high water management cost and environmental pollution in aquaculture, improve the physical, chemical and biological conditions of the aquaculture water and enhance the stability of the aquaculture water environment.

为了实现上述目的,本发明提供了一种养殖池塘的水体净化方法,该方法包括:In order to achieve the above object, the invention provides a method for purifying water in a culture pond, the method comprising:

步骤1用水泵将养殖池塘中央底层的养殖废水提升至一水槽中;Step 1: Lift the culture wastewater at the bottom of the center of the culture pond into a water tank with a water pump;

步骤2在所述水槽中分离出养殖废水中的悬浮有机物;Step 2 is to separate the suspended organic matter in the culture wastewater in the tank;

步骤3将分离出悬浮有机物的养殖废水经自然光化学催化氧化处理后,再返回到所述养殖池塘,形成水循环。In step 3, the culture wastewater from which the suspended organic matter has been separated is subjected to natural photochemical catalytic oxidation treatment, and then returned to the culture pond to form a water cycle.

本发明的水体净化方法是利用浅层沉淀原理来分离养殖废水中的悬浮有机物。浅层水的深度一般在0.3-0.6米,停留时间为20-40分钟左右,出水速度为0.7-1.5m3/m.h,在近于“零”速的条件下进行固液分离。所述的自然光化学催化氧化过程产生活性氧自由基和曝气起到脱氮解毒和补氧抑藻抑菌的作用。该自然光化学催化氧化在一斜面上进行,斜面的坡度约30-60度,斜面上水层为重力片流,流程大于1米,水层厚度小于0.3毫米。浅层水槽中净化后的养殖废水经所述斜面再返回到所述养殖池塘。在进行所述水循环的同时,由所述养殖池塘周围设置的增氧机使所述养殖池塘的水产生水平环流,依据涡流和密度差分层的水力学原理,形成了养殖池塘中央底层水的相对静止,有助于有机残渣向池中心汇集。The water body purification method of the present invention utilizes the principle of shallow sedimentation to separate the suspended organic matter in the aquaculture wastewater. The depth of shallow water is generally 0.3-0.6 meters, the residence time is about 20-40 minutes, the water outlet speed is 0.7-1.5m 3 /mh, and the solid-liquid separation is carried out under the condition of near "zero" speed. The natural photochemical catalytic oxidation process generates active oxygen free radicals and aeration plays the roles of denitrification and detoxification, oxygen supplementation, algae inhibition and bacteriostasis. The natural photochemical catalytic oxidation is carried out on a slope with a slope of about 30-60 degrees. The water layer on the slope is a gravity sheet flow, the flow is greater than 1 meter, and the thickness of the water layer is less than 0.3 mm. The purified aquaculture wastewater in the shallow water tank returns to the aquaculture pond through the slope. While carrying out the water circulation, the water in the culture pond is generated by the aeration machine arranged around the culture pond to generate a horizontal circulation, and according to the hydraulic principle of the eddy current and the density difference layer, the relative density of the bottom water in the center of the culture pond is formed. Still, it helps organic residues to pool to the center of the pool.

本发明根据养殖污水中杂质的化学、物理性质和水力学原理,利用薄水层自然光化学催化氧化原理脱氮解毒和补氧抑藻抑菌,采用水力学聚污和动力引污方式造成池塘水体良好混合并改善底层水环境条件,利用浅层沉淀原理分离水中悬浮有机物,利用光化学产氧和大气自然复氧的方式为水体增氧,养殖污泥在槽内自然脱水干化,养殖废水经过循环处理全部回用于养殖不再外排。另外,少量有机干化污泥从处理设施中清除可作为农业有机肥资源就地利用。实现了循环水养殖及养殖污水的“零排放”,是满足环保要求的一种多功能、低成本、效果好的水体净化方法,适合于海、淡水池塘养殖的水质管理。According to the chemical and physical properties and hydraulic principles of impurities in the aquaculture sewage, the present invention utilizes the principle of natural photochemical catalytic oxidation of the thin water layer to denitrify and detoxify, supplement oxygen, inhibit algae and inhibit bacteria, and adopt hydraulic pollution accumulation and dynamic sewage introduction to form pond water Mix well and improve the environmental conditions of the bottom water, use the principle of shallow sedimentation to separate suspended organic matter in the water, use photochemical oxygen generation and atmospheric natural reoxygenation to increase oxygen in the water body, and the breeding sludge is naturally dehydrated and dried in the tank, and the breeding wastewater is recycled All the processing will be reused for breeding and no longer discharged. In addition, a small amount of organic dry sludge removed from the treatment facilities can be used as agricultural organic fertilizer resources on site. It realizes the "zero discharge" of circulating aquaculture and aquaculture sewage. It is a multi-functional, low-cost, and effective water purification method that meets environmental protection requirements. It is suitable for water quality management of sea and freshwater pond aquaculture.

附图说明Description of drawings

图1是本发明水体净化方法的系统示意图。Fig. 1 is a schematic diagram of the system of the water purification method of the present invention.

图2是本发明采用净化水再分配沟的水体净化方法的系统示意图。Fig. 2 is a system schematic diagram of the water body purification method using the purified water redistribution ditch in the present invention.

具体实施方式Detailed ways

以下结合附图对本发明做进一步地详细说明。The present invention will be described in further detail below in conjunction with the accompanying drawings.

参见图1,本发明的水体净化方法可通过在平缓锅底型的水产养殖池塘1中央底部设置的集污管装置2、中央排污管3、水泵4、输水管5、布水装置6、浅层沉淀水槽7和光化斜面8组成的的自然光循环水净化系统来实现。集污管装置2由8条穿孔集污硬塑管和1条引排污管组成,用于汇集池底残渣和劣质底层。中央排污管3是一条插口硬塑管,可使较高有机负荷的废水和残渣由水泵4经输水管5提升到浅层沉淀水槽7中。水浅层沉淀水槽7和薄水层光化斜面8与养殖池塘1的坝体一体建造,浅层沉淀水槽7位于养殖池塘1的边坝上,光化斜面8则由养殖池塘1的边坡构成。浅层沉淀水槽7的深度在0.5米左右,光化斜面8的坡度为45度左右,宽度(即其上液体的流程)为1.5m。布水装置6可为多孔管布水装置,以使养殖废水在浅层沉淀水槽7长向分布。Referring to Fig. 1, the water body purification method of the present invention can pass through the sewage collection pipe device 2, the central sewage discharge pipe 3, the water pump 4, the water delivery pipe 5, the water distributing device 6, the shallow water pipe device 2 that are arranged at the central bottom of the aquaculture pond 1 of the gentle pot bottom type. The natural light circulation water purification system composed of layer sedimentation tank 7 and actinic slope 8 is realized. The sewage collection pipe device 2 is composed of 8 perforated sewage collection hard plastic pipes and 1 sewage discharge pipe, which is used to collect the residue at the bottom of the pool and the bottom layer of inferior quality. The central blowdown pipe 3 is a socket hard plastic pipe, which can make waste water and residues with higher organic loads be lifted into the shallow sedimentation tank 7 by the water pump 4 through the water delivery pipe 5 . The water shallow sedimentation tank 7 and the thin water layer actinic slope 8 are integrated with the dam body of the culture pond 1, the shallow sedimentation tank 7 is located on the side dam of the culture pond 1, and the actinization slope 8 is formed by the side slope of the culture pond 1 constitute. The depth of the shallow sedimentation tank 7 is about 0.5 meters, the slope of the actinic slope 8 is about 45 degrees, and the width (that is, the flow of the liquid on it) is 1.5 m. The water distribution device 6 can be a porous tube water distribution device, so that the culture wastewater is distributed longitudinally in the shallow sedimentation tank 7 .

运行时水泵4将养殖池塘1中央底层的高浓度养殖废水提升至浅层沉淀水槽7,通过多孔管布水装置6使养殖废水在浅层沉淀水槽7长向分布,在此进行固液分离,去除悬浮有机物。其中浅层水的深度在0.4-0.5米,停留时间为30分钟,出水速度为1.0m3/m.h,在近于“零”速的条件下进行固液分离。另外,浅层沉淀水槽7中去除悬浮有机物的同时,也可进行部分自然光化学催化氧化作用。去除悬浮有机物的养殖废水以薄水层溢出沿宽向以不超过0.3毫米的厚度流经斜面8,在此经薄水层自然光化学催化氧化脱氮解毒及补氧抑藻抑菌使水再生,然后回到养殖池塘1中循环使用。另外,由养殖池塘1周围布置的增氧机(图中未示出)造成了水平环流,依据涡流和密度差分层的水力学原理,形成了养殖池塘1中央底层水的相对静止,有助于有机残渣向池中心汇集;再经集污管装置2使较高有机负荷的废水和残渣由水泵4提升到浅层沉淀水槽7,由此形成水体的循环。During operation, the water pump 4 lifts the high-concentration aquaculture wastewater in the central bottom of the aquaculture pond 1 to the shallow sedimentation tank 7, and distributes the aquaculture wastewater in the shallow sedimentation tank 7 in the longitudinal direction through the porous pipe water distribution device 6, where solid-liquid separation is performed. Remove suspended organic matter. The depth of the shallow water is 0.4-0.5 meters, the residence time is 30 minutes, the water outlet velocity is 1.0m 3 /mh, and the solid-liquid separation is carried out under the condition of near "zero" velocity. In addition, while the suspended organic matter is removed in the shallow sedimentation tank 7, part of the natural photochemical catalytic oxidation can also be performed. The aquaculture wastewater that removes suspended organic matter overflows with a thin water layer and flows through the inclined plane 8 along the width direction with a thickness of no more than 0.3 mm, where the thin water layer is naturally photochemically catalyzed to oxidize, denitrify, detoxify, supplement oxygen, inhibit algae, and inhibit bacteria to regenerate the water. Then get back to the breeding pond 1 for recycling. In addition, the horizontal circulation is caused by the aerator (not shown) arranged around the culture pond 1. According to the hydraulic principle of the eddy current and the density difference layer, the relative stillness of the bottom water in the center of the culture pond 1 is formed, which contributes to The organic residues are collected to the center of the pool; and then the waste water and residues with higher organic loads are lifted by the water pump 4 to the shallow sedimentation tank 7 through the sewage collecting pipe device 2, thereby forming the circulation of the water body.

参见图2,为了将净化处理后的养殖废水或冲洗塘废水能够再分配到其它养殖池塘中,可在浅层沉淀水槽7和光滑斜面8之间设置一条净化水再分配沟9。由浅层沉淀水槽7溢出的去除有机悬浮物的养殖废水先进入净化水再分配沟9,再由净化水再分配沟9溢出到光滑斜面8上。其中部分或全部经浅层沉淀水槽7处理的水可由0.15米宽净化水再分配沟9经一闸管10输送到其它养殖池塘中使用。另外,还可在浅层沉淀水槽7和净化水再分配沟9之间设有分层排水管口(图中未示出)。Referring to FIG. 2 , in order to redistribute the purified aquaculture wastewater or flushing pond wastewater to other aquaculture ponds, a purified water redistribution ditch 9 can be set between the shallow sedimentation tank 7 and the smooth slope 8 . The aquaculture wastewater overflowing from the shallow sedimentation tank 7 to remove organic suspended matter first enters the purified water redistribution ditch 9 , and then overflows onto the smooth slope 8 by the purified water redistribution ditch 9 . Wherein part or all of the water processed by the shallow sedimentation tank 7 can be transported to other culture ponds by a 0.15 meter wide purified water redistribution ditch 9 through a lock tube 10 for use. In addition, a layered drain outlet (not shown in the figure) may also be provided between the shallow sedimentation tank 7 and the purified water redistribution ditch 9 .

在池塘养殖前期,该水体净化系统不需运行。这时的浅层沉淀水槽7作为污泥自然干化池使用,上述养殖废水循环净化时沉淀于槽中的有机污泥经自然脱水后成为固态,人工铲出用于林木有机肥资源化利用。In the early stage of pond culture, the water purification system does not need to be operated. At this time, the shallow sedimentation tank 7 is used as a sludge natural drying tank. The organic sludge deposited in the tank during the circulation and purification of the above-mentioned aquaculture wastewater becomes solid after natural dehydration, and is manually shoveled out for resource utilization of forest organic fertilizer.

使用上述装置,既可满足水产养殖对水环境质量的要求,又能防止由于养殖废水排放造成的环境污染问题产生。The above-mentioned device can not only meet the requirements of aquaculture for water environment quality, but also prevent the occurrence of environmental pollution problems caused by the discharge of aquaculture wastewater.

本发明通过采用浅层沉淀分离水中悬浮有机物和薄水层自然光化学催化氧化脱氮解毒及补氧抑藻抑菌使水再生,净化后的富氧水自流回到养殖池中循环使用,造成池中水的垂直流动。这种水循环方式形成了养殖池中水的整体流动,有利于打破水体分层现象,改善塘底环境质量。The present invention regenerates the water by adopting shallow sedimentation to separate the suspended organic matter in the water and the natural photochemical catalysis of the thin water layer, denitrification and detoxification, supplementing oxygen, inhibiting algae and inhibiting bacteria, and the purified oxygen-enriched water flows back to the culture pond for recycling, resulting in a pond vertical flow of water. This water circulation mode forms the overall flow of water in the aquaculture pond, which is conducive to breaking the stratification of the water body and improving the environmental quality of the pond bottom.

参见表1~3,通过对处理前后化学需氧量(COD),悬浮物(SS)、“三N”和磷酸盐的测定,可看出本发明的水体净化方法能够降低养殖水体的溶解性氨态氮、亚硝态氮、硝态氮,以及悬浮物和有机物。其中的进水是指浅层沉淀水槽7的入口位置的水体,出水是指经斜面8返回养殖池塘1的水体。Referring to Tables 1 to 3, by chemical oxygen demand (COD) before and after treatment, suspended solids (SS), "three N" and phosphate measurements, it can be seen that the water purification method of the present invention can reduce the solubility of aquaculture water Ammonia nitrogen, nitrite nitrogen, nitrate nitrogen, and suspended solids and organic matter. Water inflow wherein refers to the water body of the inlet position of shallow sedimentation tank 7, and water outfall refers to the water body that returns to culture pond 1 through inclined plane 8.

表1对废水中COD的去除效果   COD测定次数   进水mg/l   出水mg/l   去除率%   1   383.6   284.6   25.81   2   318.6   207.3   34.93   3   358.8   262.4   26.86   4   375.2   287.0   23.51   5   392.2   297.8   23.77   平均去除率   26.98 Table 1 to the removal effect of COD in wastewater COD measurement times Influent mg/l Effluent mg/l Removal rate% 1 383.6 284.6 25.81 2 318.6 207.3 34.93 3 358.8 262.4 26.86 4 375.2 287.0 23.51 5 392.2 297.8 23.77 average removal rate 26.98

表2对废水中SS的去除效果   SS测定次数   进水mg/l   出水mg/l   去除率%   1   182.5   30.5   83.29   2   186.5   27.5   85.25   3   180.2   33.0   81.69   4   187.8   40.0   78.70   5   194.0   41.5   78.61   平均去除率   81.51 Table 2 to the removal effect of SS in wastewater SS measurement times Influent mg/l Effluent mg/l Removal rate% 1 182.5 30.5 83.29 2 186.5 27.5 85.25 3 180.2 33.0 81.69 4 187.8 40.0 78.70 5 194.0 41.5 78.61 average removal rate 81.51

表3对废水中“三N”和磷酸盐的去除效果   项目   进水mg/l   出水mg/l   去除率%   硝酸盐态氮   0.4190-0.5575   0.3705-0.4325   10.37-27.35   亚硝酸盐态氮   0.0550-0.1526   0.0218-0.0488   22.45-44.74   氨态氮   0.1632-0.4355   0.0337-0.2775   13.39-79.53   磷酸盐   0.1580-0.1920   0.0960-0.1070   39.24-44.27 Table 3 Removal effect of "three N" and phosphate in wastewater project Influent mg/l Effluent mg/l Removal rate% Nitrate nitrogen 0.4190-0.5575 0.3705-0.4325 10.37-27.35 Nitrite nitrogen 0.0550-0.1526 0.0218-0.0488 22.45-44.74 Ammonia nitrogen 0.1632-0.4355 0.0337-0.2775 13.39-79.53 Phosphate 0.1580-0.1920 0.0960-0.1070 39.24-44.27

另外,还对塘底水中亚硝酸盐态氮进行了测定,采用本发明水体净化方法的养殖池塘底层水中亚硝酸盐态氮浓度为0.1628-0.1666毫克/升,而对照养殖池塘底层水中亚硝酸盐氮浓度为0.4307-0.4492毫克/升。由此可见,本发明的水体净化方法大大改善了养殖池塘的水体质量。In addition, the nitrite nitrogen in the bottom water of the pond was also measured, and the concentration of nitrite nitrogen in the bottom water of the culture pond by the water purification method of the present invention was 0.1628-0.1666 mg/liter, while the nitrite concentration in the bottom water of the culture pond was 0.1628-0.1666 mg/liter. The nitrogen concentration is 0.4307-0.4492 mg/L. It can be seen that the water body purification method of the present invention has greatly improved the water quality of the culture pond.

最后应当说明的是:以上实施例仅用以说明本发明的技术方案而非对其限制;尽管参照较佳实施例对本发明进行了详细的说明,所属领域的普通技术人员应当理解:依然可以对本发明的具体实施方式进行修改或者对部分技术特征进行等同替换;而不脱离本发明技术方案的精神,其均应涵盖在本发明请求保护的技术方案范围当中。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present invention and not to limit them; although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that: the present invention can still be Modifications to the specific implementation of the invention or equivalent replacement of some technical features; without departing from the spirit of the technical solution of the present invention, should be included in the scope of the technical solution claimed in the present invention.

Claims (10)

1, a kind of water body purification method of cultivating pool comprises:
Step 1 is rested the breeding wastewater of growing pond central authorities bottom with water pump and is promoted in the tank;
Step 2 is isolated the suspended organic matter in the breeding wastewater in described tank;
Step 3 will be isolated the breeding wastewater of suspended organic matter after the natural light chemical catalytic oxidation is handled, and turn back to described cultivating pool again, form water cycle.
2, water body purification method according to claim 1, in the wherein said step 2, suspended organic matter is to adopt the shallow layer precipitating method in the described separation breeding wastewater.
3, water body purification method according to claim 2, in the wherein said shallow layer precipitating method, the degree of depth of shallow seated groundwater is a 0.3-0.6 rice, and the residence time is 20-40 minute, and going out water speed is 0.7-1.5m 3/ m.h.
4, water body purification method according to claim 3, the degree of depth of wherein said shallow seated groundwater are 0.4-0.5 rice, and the residence time is 30 minutes, and going out water speed is 1.0m 3/ m.h.
5, water body purification method according to claim 1, wherein said natural light chemical catalytic oxidation comprise the breeding wastewater of the isolating suspended organic matter inclined-plane of flowing through.
6, water body purification method according to claim 5, wherein the gradient on the inclined-plane of Cai Yonging is the 30-60 degree.
7, water body purification method according to claim 6, wherein the gradient on the inclined-plane of Cai Yonging is 45 degree.
8, water body purification method according to claim 5, the wherein said flow process of breeding wastewater on described inclined-plane of isolating suspended organic matter is greater than 1 meter, and thickness is less than 0.3 millimeter.
9, water body purification method according to claim 5, wherein the dam body of inclined-plane of Cai Yonging and tank and cultivating pool is an one.
10, according to each described water body purification method of claim 1~9, wherein when carrying out described water cycle, make the horizontal circulation of water generates of described cultivating pool by the oxygenating machine that is provided with around the described cultivating pool, form the static relatively of described cultivating pool central authorities bottom water.
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CN101891332B (en) * 2009-05-18 2011-12-28 上海市水产技术推广站 Facility for treating pond culture wastewater
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CN110203999B (en) * 2019-06-18 2020-10-20 联科华技术股份有限公司 Sunlight fishpond circulation purification system
CN111908550A (en) * 2020-04-20 2020-11-10 广州埃米石墨烯科技有限公司 Method and device for purifying aquaculture water
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