EFFICIENT NITROGEN AND PHOSPHORUS REMOVAL PROCESS SYSTEM FOR MARICULTURE TAIL WATER TREATMENT

Abstract

Disclosed is an efficient nitrogen and phosphorus removal process system for mariculture tail water treatment. The process system comprises a physical filtering device, an efficient biological treatment unit, a flocculation sedimentation tank, a sand filtering tank, a clean water tank and a sludge tank, wherein the physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank, the sand filtering tank and the clean water tank are sequentially connected; the physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank and the sand filtering tank are all connected with the sludge tank through pipelines, and the physical filtering device and the sand filtering tank are both connected with the clean water tank through pipelines. The efficient biological treatment unit is filled with a modified high-hydrophilic wear-resistant filler, and the whole system is provided with a carbon source, a flocculation agent and a directional Phoslock dosing device.

Claims

1. An efficient nitrogen and phosphorus removal process system for mariculture tail water treatment, comprising a physical filtering device, an efficient biological treatment unit, a flocculation sedimentation tank, a sand filtering tank, a clean water tank and a sludge tank, wherein the physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank, the sand filtering tank and the clean water tank are sequentially connected; the physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank and the sand filtering tank are all connected with the sludge tank through pipelines; and the physical filtering device and the sand filtering tank are both connected with the clean water tank through pipelines.

2. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein the efficient biological treatment unit comprises a biological aerated filter 1, an anaerobic tank, a biological aerated filter 2, a modified high-hydrophilic wear-resistant filler and a glass fiber reinforced plastic grid cover plate, the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2 are sequentially connected, the modified high-hydrophilic wear-resistant filler is filled in the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2, the glass fiber reinforced plastic grid cover plate is located at the upper parts of the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2, and the filler is pressed to prevent floating.

3. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein the tank volume ratio of the biological aerated filter 1, the anaerobic tank to the biological aerated filter 2 is 2:4:1, the filling volume of the modified high-hydrophilic wear-resistant filler in the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2 is not less than 60% of the tank volume, and the biological aerated filter and the anaerobic tank are respectively inoculated with efficient salt-tolerant nitrifying bacteria and denitrifying bacteria.

4. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein a microporous aeration disc is installed at the bottom of the biological aerated filter, a blower is added to aerate the interior of the tank, a diving mixer is installed in the anaerobic tank and is made of an anticorrosive material, and an external carbon source dosing device of the anaerobic tank is used as an emergency carbon source supplementary device.

5. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 2, wherein the modified high-hydrophilic wear-resistant filler is made of polyurethane as a carrier of microorganisms by adopting a suspended ball combined filler method, the carrier material is provided with active groups such as amino, carboxyl, epoxy and other groups, the void ratio is over 96%, the specific surface area is 6000-15000 m.sup.2/m.sup.3, the density of immobilized microorganisms is close to that of water, and the immobilized microorganisms are suspended in water.

6. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 3, wherein the modified high-hydrophilic wear-resistant filler is made of polyurethane as a carrier of microorganisms by adopting a suspended ball combined filler method, the carrier material is provided with active groups such as amino, carboxyl, epoxy and other groups, the void ratio is over 96%, the specific surface area is 6000-15000 m.sup.2/m.sup.3, the density of immobilized microorganisms is close to that of water, and the immobilized microorganisms are suspended in water.

7. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein the flocculation sedimentation tank is externally connected with an agent dosing device, and the agent mainly comprises polyaluminum chloride (PAC) and polyacrylamide (PAM) and is added with auxiliary lanthanum-containing directional Phoslock.

8. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein the physical filtering device can be a microfiltration machine, a curved screen and other devices with an automatic backwashing function and is installed on a biological tank.

9. The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment according to claim 1, wherein in the process system, except that the water body is lifted by a pump once before the physical filtering device, all subsequent water bodies are realized by gravity.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0024] FIG. 1 is a structural schematic diagram of the present disclosure.

[0025] FIG. 2 is a diagram of a modified high-hydrophilic wear-resistant filler.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0026] The following clearly and completely describes the technical scheme in the embodiments of the present disclosure with reference to the attached figures in the embodiments of the present disclosure. Apparently, the described embodiments are merely a part rather than all of the embodiments of the present disclosure. The following description of at least one exemplary embodiment is merely illustrative and definitely is not construed as any limitation on the present disclosure and use of the present disclosure. All other embodiments obtained by those skilled in the art based on the embodiments of the present disclosure without creative efforts shall fall within the protection scope of the present disclosure.

Embodiment I

[0027] Referring to FIG. 1, the present disclosure provides an efficient nitrogen and phosphorus removal process system for mariculture tail water treatment. The process system comprises a physical filtering device, an efficient biological treatment unit, a flocculation sedimentation tank, a sand filtering tank, a clean water tank and a sludge tank. The physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank, the sand filtering tank and the clean water tank are sequentially connected. The physical filtering device, the efficient biological treatment unit, the flocculation sedimentation tank and the sand filtering tank are all connected with the sludge tank through pipelines. The physical filtering device and the sand filtering tank are both connected with the clean water tank through pipelines.

[0028] The efficient biological treatment unit comprises a biological aerated filter 1, an anaerobic tank, a biological aerated filter 2, a modified high-hydrophilic wear-resistant filler and a glass fiber reinforced plastic grid cover plate. The biological aerated filter 1, the anaerobic tank and the biological aerated filter 2 are sequentially connected. The modified high-hydrophilic wear-resistant filler is filled in the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2. The glass fiber reinforced plastic grid cover plate is located at the upper parts of the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2. The filler is pressed to prevent floating.

[0029] The tank volume ratio of the biological aerated filter 1, the anaerobic tank to the biological aerated filter 2 is 2:4:1. The filling volume of the modified high-hydrophilic wear-resistant filler in the biological aerated filter 1, the anaerobic tank and the biological aerated filter 2 is not less than 60% of the tank volume. The biological aerated filter and the anaerobic tank are respectively inoculated with efficient salt-tolerant nitrifying bacteria and denitrifying bacteria.

[0030] A microporous aeration disc is installed at the bottom of the biological aerated filter. A blower is added to aerate the interior of the tank. A diving mixer is installed in the anaerobic tank and is made of 316L stainless steel. An external carbon source dosing device of the anaerobic tank is used as an emergency carbon source supplementary device. The common carbon sources comprise glucose, methyl alcohol, ethyl alcohol, sodium acetate, corn starch and the like.

[0031] The modified high-hydrophilic wear-resistant filler is made of polyurethane as a carrier of microorganisms by adopting a suspended ball combined filler method. The carrier material is provided with active groups such as amino, carboxyl, epoxy and other groups. The void ratio is over 96%. The specific surface area is 6000-15000 m.sup.2/m.sup.3. The density of immobilized microorganisms is close to that of water, and the immobilized microorganisms are suspended in water.

[0032] The flocculation sedimentation tank is externally connected with an agent dosing device, and the agent mainly comprises polyaluminum chloride (PAC) and polyacrylamide (PAM) and is added with auxiliary lanthanum-containing directional Phoslock.

[0033] The physical filtering device can be a microfiltration machine, a curved screen and other devices with an automatic backwashing function, and the device is installed on a biological tank.

[0034] In the working process of the process system, the discharged water from a mariculture pond or a factory culture pond is extracted once by a water pump and enters a physical filtering device (such as a microfilter). The filtered water enters the biological aerated filter 1, and the backwashing water containing large particles enters a sludge pond. In the biological aerated filter 1, the solution protein and ammonia nitrogen in the water can be converted into nitrite nitrogen under the action of nitrifying bacteria and further converted into nitrate nitrogen. The overflow water from the biological aerated filter 1 enters the anaerobic tank, and the nitrate nitrogen and nitrite nitrogen in the water body are converted into nitrogen under the action of denitrifying bacteria, so that denitrification is realized, and meanwhile, refractory organic substances (such as antibiotics and other drugs) can be hydrolyzed. The overflow water from the upper part of the biological aerated filter 2 enters the flocculation sedimentation tank, and microorganisms decompose organic matters to reduce COD. At the same time, phosphorus accumulating bacteria realize aerobic phosphorus absorption. The overflow water from the upper part of the biological aerated filter 2 enters the flocculation sedimentation tank, and a small amount of lanthanum-containing directional Phoslock is added to realize the deep removal of phosphorus in the water body. Under the action of flocculants such as PAC and PAM, phosphorus is settled to the bottom of the tank body and enters the sludge tank through the sludge discharge pipe. The overflow water from the upper part of the flocculation sedimentation tank enters the sand filtering tank, is further filtered by quartz sand and then enters the clean water tank. The sand filtering tank is cleaned regularly, and the backwashed filter residue enters the sludge tank. The water in the clean water tank can be recycled or discharged up to the standard, and at the same time, clean water for backwashing can be provided for the physical filtering device and sand filtering tank. A sludge hopper is arranged at the bottom of the sludge tank. As the sludge yield is small, sludge is discharged only by gravity compression. The water quality treated by this process system can meet the first-class standard requirements in the Discharge Requirements of Mariculture Water (SC/T9103-2007).

Embodiment II

[0035] The efficient nitrogen and phosphorus removal process system for mariculture tail water treatment is used for treating the industrial aquaculture tail water of South American shrimps in Hainan, and the treated effluent water quality meets the first-class standard requirements in the Discharge Requirements of Mariculture Water (SC/T9103-2007). The water quality indexes of inflow and effluent water are as follows through the monitoring data of a third party:

TABLE-US-00001 First-class standard Inflow Effluent Serial requirements in water water numbers Indexes Units SC/T9103-2007 quality quality 1 pH Dimensionless 7.0-8.5 7.5 7.09 2 Chemical oxygen mg/L ≤10 1.4 2.7 demand (COD.sub.Mn) 3 Biochemical oxygen mg/L ≤6 4 3 demand (BOD.sub.5) 4 Active phosphorus mg/L ≤0.05 0.078 0.008 (in terms of P) 5 Ammonia Inorganic mg/L ≤0.5 21 0.343 nitrogen 6 Copper Nitrate mg/L ≤0.1 0.0013 0.0009 7 Zinc Nitrite mg/L ≤0.2 0.082 0.073 Note: inflow water refers to the aquaculture tail water discharged from the culture pond, and effluent water refers to the discharged water treated by treatment facilities.

[0036] Therefore, it is observed that after the mariculture tail water is treated by the process system, all indexes can meet the first-class standard requirements in the Discharge Requirements of Mariculture Water (SC/T9103-2007), and the standard discharge can be achieved.

[0037] Although the specific embodiments of the present disclosure have been described above, those skilled in the art should understand that the specific embodiments we have described are only illustrative, only used for explaining the present disclosure, but not for limiting the present disclosure. Obvious changes or variations which belong to the technical scheme of the present disclosure are still within the scope of protection of the present disclosure.