CN101323496A - Scale hogpen sewage disposal method and integrated equipment thereof - Google Patents
Scale hogpen sewage disposal method and integrated equipment thereof Download PDFInfo
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- CN101323496A CN101323496A CNA2008101200989A CN200810120098A CN101323496A CN 101323496 A CN101323496 A CN 101323496A CN A2008101200989 A CNA2008101200989 A CN A2008101200989A CN 200810120098 A CN200810120098 A CN 200810120098A CN 101323496 A CN101323496 A CN 101323496A
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- storehouse
- cylindrical shell
- biological respinse
- sewage
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- 239000010865 sewage Substances 0.000 title claims abstract description 69
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 39
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 32
- 239000012528 membrane Substances 0.000 claims abstract description 29
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 26
- 241000282898 Sus scrofa Species 0.000 claims description 38
- 238000005374 membrane filtration Methods 0.000 claims description 30
- 230000003647 oxidation Effects 0.000 claims description 30
- 230000003197 catalytic Effects 0.000 claims description 29
- 238000005276 aerator Methods 0.000 claims description 26
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 22
- 230000001954 sterilising Effects 0.000 claims description 22
- 238000001471 micro-filtration Methods 0.000 claims description 18
- 239000000463 material Substances 0.000 claims description 15
- 210000000188 Diaphragm Anatomy 0.000 claims description 14
- 239000010802 sludge Substances 0.000 claims description 12
- 229910052742 iron Inorganic materials 0.000 claims description 11
- 238000005842 biochemical reaction Methods 0.000 claims description 9
- 239000003206 sterilizing agent Substances 0.000 claims description 5
- ZKQDCIXGCQPQNV-UHFFFAOYSA-N Calcium hypochlorite Chemical compound [Ca+2].Cl[O-].Cl[O-] ZKQDCIXGCQPQNV-UHFFFAOYSA-N 0.000 claims description 2
- 239000003344 environmental pollutant Substances 0.000 abstract description 10
- 231100000719 pollutant Toxicity 0.000 abstract description 10
- 230000001488 breeding Effects 0.000 abstract description 8
- 244000144972 livestock Species 0.000 abstract description 8
- 244000144977 poultry Species 0.000 abstract description 8
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 230000000249 desinfective Effects 0.000 abstract description 4
- 230000000875 corresponding Effects 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 abstract 4
- 229920002521 Macromolecule Polymers 0.000 abstract 1
- 238000005273 aeration Methods 0.000 abstract 1
- 238000006065 biodegradation reaction Methods 0.000 abstract 1
- 238000004042 decolorization Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000011148 porous material Substances 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 13
- 230000015556 catabolic process Effects 0.000 description 8
- 230000004059 degradation Effects 0.000 description 8
- 238000006731 degradation reaction Methods 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 6
- 239000002689 soil Substances 0.000 description 5
- 230000002550 fecal Effects 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- 238000009360 aquaculture Methods 0.000 description 3
- 244000144974 aquaculture Species 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 241000276438 Gadus morhua Species 0.000 description 2
- 210000002700 Urine Anatomy 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 235000019516 cod Nutrition 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000011150 reinforced concrete Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 206010059410 Faecaluria Diseases 0.000 description 1
- 210000003608 Feces Anatomy 0.000 description 1
- 239000004567 concrete Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003102 growth factor Substances 0.000 description 1
- 239000010871 livestock manure Substances 0.000 description 1
- -1 nitrogen phosphorus Chemical compound 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Abstract
The invention discloses a scale pig-farm sewage disposal method and a corresponding integrated apparatus. The method adopts a biological reaction bin (1), a membrane filtering bin (2), an anaerobic hydrolysis bin (3), a contact oxidization bin (4) and a disinfection bin (5) so as to sequentially carry out biochemistry reaction, membrane filtering and hydrolysis membrane filtering to filter parts of undegraded macromolecule from water, and also biodegradation and decolorization and disinfection processes, thus leading the water to completely reach the discharge standard of 'Discharge Standard of Pollutants for Livestock and Poultry Breeding'. And besides the biological reaction bin (1), the membrane filtering bin (2), the anaerobic hydrolysis bin (3), the contact oxidization bin (4) and the disinfection bin (5), the integrated apparatus used for realizing the method also includes a pore aeration device (7), a micro filter-membrane element (9) and a pump I (8), a pump II (10) and a pump III (11) which are arranged in an apparatus bin (6). The apparatus of the invention can carry out the integrated harmless disposal for the sewage of the scale pig-farm.
Description
Technical field:
The present invention relates to the high-concentration culture technical field of sewage, specifically is to make it reach scale pig farm sewage water treatment method and integrated-type equipment thereof that " livestock and poultry breeding industry pollutant emission standard " requires after a kind of pig farm sewage directly can the processing.
Background technology:
Large scale of pig farm field sewage is a most typical pollutant in the aquaculture waste, and it mainly comprises pig urine, part pig manure and pig house wash-down water, belongs to high concentrated organic wastewater.Because described large scale of pig farm field sewage is the important source of aquaculture environmental pollution, therefore, how large scale of pig farm field sewage being carried out harmless treatment has become scale pig farm aquaculture in recent years and has been badly in need of the problem researched and solved.
At present, the sewage harmless treatment of scale pig farm mainly contains also field processing, handles naturally and three kinds of tupes of industrial treatment, wherein, also the field tupe is a kind of traditional, cost-effective method of disposal, it is that fecaluria, wash-down water are imposed in the soil, organic substance is decomposed changes into soil ulmin and plant growth factor, and organonitrogen phosphorus changes into inorganic nitrogen phosphorus, thereby realize the recycle of nutrient, reach zero release of pollutant.But this pattern only is applicable to away from the city, and the soil broadness has the dissolve large scale of pig farm field of fecal sewage, enough farmlands.What the nature tupe adopted is natural treatment systems such as oxidation pond, artificial swamp.Although natural tupe also can reach the similar also effect of field tupe; but it also can only be applicable to away from the city; the large scale of pig farm field of soil broadness particularly has beach, wasteland, forest land or bottom land can do the large scale of pig farm field of sewage natural treatment system.
Along with increasing progressively day by day of population, soil in short supply day by day, the industrial treatment pattern is progressively replacing the status of going back field tupe and natural tupe, its reason just is, the enforcement of industrial treatment pattern need not to rely on a large amount of farmlands fecal sewage of dissolving, and also need not to rely on beach, wasteland, forest land or bottom land and makes the sewage natural treatment system.At present, Granted publication number is handled the anaerobic reactor that contains high-concentration suspension solid waste water for the utility model patent of CN1269744C discloses a kind of industrial treatment pattern that adopts, and it is applicable to that Wastewater from Pig Farm, excrement and urine water, excess sludge etc. contain the Anaerobic Digestion of high-concentration suspension solid (high-concentration suspension solid SS is 1%～10%) waste water.This anaerobic reactor is by reactor body, gas extractor, automatic control system and advance, four parts of water exhaust system constitute; Described reactor master ladder is a cylindrical reinforced concrete pond; Described cylindrical reinforced concrete is provided with agitator in the pond; Concrete sump pool wall upper part is set to an annular seal-water tank; Floating bell jar is placed in the annular seal-water tank of pool wall upper end; Gas collection pipe is contained in the floating bell jar center of top; Advance, water-freeing arrangement and pond body connect; Automatic control device is controlled slush pump, agitator and sump pump respectively and is opened and close.Tupe that the disclosed anaerobic reactor of above-mentioned utility model patent adopts and other industrial treatment pattern have a common drawback, be that they can only carry out a kind of processing of strengthening the anaerobic treatment or a certain local unit of pig farm sewage, also can't make water outlet after the processing reach the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully.
Summary of the invention:
The technical problem to be solved in the present invention is, provide a kind of under the situation that need not a large amount of farmlands, beach, wasteland, forest land or bottom land, can carry out effective integrated harmless treatment to scale pig farm sewage, thereby make water outlet after the processing reach the scale pig farm sewage water treatment method of the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully.
Technical solution of the present invention is that a kind of scale pig farm sewage water treatment method that includes following steps is provided:
1., at first make sewage in the cylindrical shell of biological respinse storehouse, carry out biochemical reaction, and make the sewage behind the biochemical reaction flow in the membrane filtration storehouse that directly is communicated with biological respinse storehouse cylindrical shell by a pipeline;
2., utilize the micro-filtration membrane module be installed in to hold back active sludge and larger molecular organics from the sewage that biological respinse Cang Tongtichu flows through in membrane filtration the storehouse in, and the membrane filtration water outlet is flowed in the anaerobic hydrolysis storehouse that is communicated with micro-filtration membrane module by the suction water pump, make the sewage that has active sludge and larger molecular organics flow back to biological respinse storehouse cylindrical shell by water pump I;
3., in the anaerobic hydrolysis storehouse, the part macromole that is not degraded in the membrane filtration water outlet is hydrolyzed, the water outlet that biochemical obviously improves after the hydrolysis is flow in the catalytic oxidation storehouse by pipeline;
4., in the catalytic oxidation storehouse to the further biodegrade of water outlet, make then water outlet by water pump II flow into the sterilization storehouse in;
5., in the sterilization storehouse, water outlet is decoloured and disinfected;
Wherein, the intravital biological concentration of described biological respinse storehouse tube is 19000mg/L～21000mg/L; Described anaerobic hydrolysis is provided with conventional biologic packing material in the storehouse, and cultivating on the described conventional biologic packing material has the anaerobe film; Described catalytic oxidation is provided with floating stuffing in the storehouse, and cultivating on the described floating stuffing has aerobic biologic membrane; Described sterilization is placed with sterilizing agent in the storehouse.
After adopting above step and feature, scale of the present invention pig farm sewage water treatment method has following remarkable advantage and beneficial effect:
1, the present invention is because what adopt also is a kind of industrial treatment pattern, therefore need not to rely on a large amount of farmlands fecal sewage of dissolving in use, also need not to rely on beach, wasteland, forest land or bottom land and makes the sewage natural treatment system;
2, in addition, the present invention is except will be in the anaerobic hydrolysis storehouse carrying out part larger molecular organics such as the Mierocrystalline cellulose that anaerobic treatment is not degraded in promptly to sewage to sewage, materials such as xylogen are hydrolyzed and do to improve outside the biochemical of sewage in order to this, not only also in the biological respinse storehouse before sewage flow into the anaerobic hydrolysis storehouse, carry out effectively catching under the effect of biochemical reaction and the micro-filtration membrane module in the membrane filtration storehouse and flow through active sludge and larger molecular organics the sewage that comes from biological respinse Cang Tongtichu, thereby improve the activated sludge concentration in the cylindrical shell of biological reflection storehouse, and, also will carry out further biological degradation in the catalytic oxidation storehouse after the anaerobic hydrolysis storehouse improves the biochemical property of sewage and in last sterilization storehouse last decolouring is carried out in water outlet and disinfected, after above-mentioned integrated efficiently harmless treatment, the water quality of water outlet can reach the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully.
As a kind of improvement of scale of the present invention pig farm sewage water treatment method, can place the iron plane flower in the described anaerobic hydrolysis storehouse; The volume ratio of described iron plane flower and biologic packing material is not higher than 0.5: 1.In the anaerobic hydrolysis storehouse, iron plane flower and biologic packing material installation volume mixed than the ratio that is not higher than 0.5: 1 can obviously strengthen the anaerobic hydrolysis storehouse, thereby further improve the degradation effect in follow-up catalytic oxidation storehouse the organic destruction of complexity.
Another technical problem that the present invention will solve is, provide a kind of under the situation that need not a large amount of farmlands, beach, wasteland, forest land or bottom land, can carry out effective integrated harmless treatment to scale pig farm sewage, thereby make water outlet after the processing reach the integrated-type equipment that is used for scale pig farm sewage water treatment method of the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully.
Another technical solution of the present invention is that provide a kind of scale pig farm sewage integrated-type with following structure to handle equipment: it comprises biological respinse storehouse cylindrical shell, membrane filtration storehouse, anaerobic hydrolysis storehouse, catalytic oxidation storehouse, sterilization storehouse and equipment compartment; Described biological respinse storehouse cylindrical shell inner bottom part is equipped with some micro-hole aerator I; Described micro-hole aerator I and gas blower are used; Middle part, described membrane filtration storehouse directly is communicated with biological respinse storehouse cylindrical shell by pipeline; Bottom, described membrane filtration storehouse is communicated with biological respinse storehouse cylindrical shell by a water pump I; Described membrane filtration is provided with micro-filtration membrane module in the storehouse; Described micro-filtration membrane module is communicated with the anaerobic hydrolysis storehouse by the suction water pump; Described anaerobic hydrolysis storehouse is communicated with the catalytic oxidation storehouse by pipeline; Described catalytic oxidation storehouse is communicated with the sterilization storehouse by water pump II; Described gas blower, water pump I, water pump II and suction water pump are installed in the equipment compartment.
After adopting above structure, the integrated-type equipment that the present invention is used for above-mentioned scale pig farm sewage water treatment method has following remarkable advantage and beneficial effect:
1, integrated-type among the present invention equipment is except can be in the anaerobic hydrolysis storehouse carrying out part larger molecular organics such as the Mierocrystalline cellulose that anaerobic treatment is not degraded in promptly to sewage to sewage, materials such as xylogen are hydrolyzed and do to improve outside the biochemical of sewage in order to this, not only can also in the biological respinse storehouse before sewage flow into the anaerobic hydrolysis storehouse, carry out effectively catching under the effect of biochemical reaction and the micro-filtration membrane module in the membrane filtration storehouse and flow through active sludge and larger molecular organics the sewage that comes from biological respinse Cang Tongtichu, thereby improve the activated sludge concentration in the cylindrical shell of biological reflection storehouse, and, can also carry out further biological degradation in the catalytic oxidation storehouse after the anaerobic hydrolysis storehouse improves the biochemical property of sewage and in last sterilization storehouse last decolouring is carried out in water outlet and disinfected, after integrated-type equipment among employing the present invention carried out above-mentioned integrated efficiently harmless treatment, the water quality of water outlet can reach the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully.
2, only need use corresponding biological respinse storehouse cylindrical shell, membrane filtration storehouse, anaerobic hydrolysis storehouse, catalytic oxidation storehouse and sterilization storehouse during the integrated-type armament-related work among the present invention, and the setting and the work in biological respinse storehouse cylindrical shell, membrane filtration storehouse, anaerobic hydrolysis storehouse, catalytic oxidation storehouse and sterilization storehouse are a large amount of farmland, beach, wasteland, forest land or bottom lands of dependence not allowable, therefore, integrated-type among the present invention equipment need not to rely on a large amount of farmlands fecal sewage of dissolving in use, also need not to rely on and makes the sewage natural treatment system.
As a kind of improvement of integrated-type equipment of the present invention, some jet aerators can be installed in the intravital top of tube, described biological respinse storehouse.Because the oxygen requirement when carrying out biochemical reaction in the cylindrical shell of biological respinse storehouse is huge, can make in the cylindrical shell of biological respinse of the present invention storehouse behind the installation jet aerator and have two aerating systems, thereby satisfy the intravital oxygen requirement requirement of biological respinse storehouse tube better, the target that the present invention is reached efficiently dispose of sewage.
Another kind as integrated-type equipment of the present invention improves, and described biological respinse storehouse cylinder inboard wall is connected with two diaphragms; The top of described diaphragm is lower than the intravital water level of biological respinse storehouse tube; The bottom of described diaphragm is higher than the bottom of biological respinse storehouse cylindrical shell; Described micro-hole aerator is between two diaphragms.Being provided with of diaphragm can force current to circulate up and down in the cylindrical shell of biological respinse storehouse, thereby further improve the duration of contact of air water, improve the oxygen transfer efficiency that jet aerator sprays air-water mixture,, save energy consumption to guarantee the huge oxygen requirement of biological respinse storehouse cylindrical shell.
As another improvement of integrated-type equipment of the present invention, bottom, described catalytic oxidation storehouse is equipped with some micro-hole aerator II; Described micro-hole aerator II and gas blower are used.Being provided with of micro-hole aerator II can guarantee to have in the catalytic oxidation storehouse enough oxygen that sewage is carried out further biological degradation.
Description of drawings:
Fig. 1 is that scale of the present invention pig farm sewage integrated-type is handled the plan structure synoptic diagram after equipment removes top cover.
Fig. 2 is the principle schematic of scale of the present invention pig farm sewage water treatment method.
Shown in the figure: 1, membrane biological reaction storehouse cylindrical shell, 2, the membrane filtration storehouse, 3, the anaerobic hydrolysis storehouse, 4, the catalytic oxidation storehouse, 5, sterilization storehouse, 6, equipment compartment, 7, micro-hole aerator I, 8, water pump I, 9, micro-filtration membrane module, 10, the suction water pump, 11, water pump II, 12, diaphragm, 13, jet aerator, 14, gas blower, 15, micro-hole aerator II, 16, conventional biologic packing material and iron plane flower mixture, 17, the anaerobe film, 18, floating stuffing, 19, aerobic biologic membrane, 20, sterilizing agent.
Specific embodiment:
The invention will be further described below in conjunction with the drawings and specific embodiments:
As shown in Figure 2, the execution of scale of the present invention pig farm sewage water treatment method may further comprise the steps: at first make sewage carry out biochemical reaction in biological respinse storehouse cylindrical shell 1, and make the sewage behind the biochemical reaction flow in the membrane filtration storehouse 2 that directly is communicated with biological respinse storehouse cylindrical shell 1 by a pipeline; Then, utilization is installed in micro-filtration membrane modules 9 in the membrane filtration storehouse 2 and holds back from biological respinse storehouse cylindrical shell 1 and flow through active sludge and larger molecular organics in the sewage that comes, and make the membrane filtration water outlet by in the anaerobic hydrolysis storehouse 3 that suction water pump 10 flows into micro-filtration membrane module 9 is communicated with, and the sewage that has active sludge and larger molecular organics is flowed back in the biological respinse storehouse cylindrical shell 1 by water pump I 8; Then, in the anaerobic hydrolysis storehouse 3 that is provided with conventional biologic packing material and iron plane flower mixture 16, utilize the part macromole that is not degraded in 17 pairs of membrane filtration water outlets of anaerobe film of cultivating on conventional biologic packing material to be hydrolyzed, and the obvious water outlet that improves of biochemical flow in the catalytic oxidation storehouse 4 after making hydrolysis by pipeline; Then, further biological degradation is carried out in 19 pairs of water outlets of aerobic biologic membrane of utilize cultivating in being provided with the catalytic oxidation storehouse 4 of floating stuffing 18 on the floating stuffing 18 of routine, and the water outlet after the biological degradation is flow in the sterilization storehouse in 5 by water pump II 11; At last, sterilizing agents 20 in the utilization sterilization storehouse 5 decolour to water outlet as Losantin and disinfect, the function in sterilization storehouse 5 is decolourings of carrying out to wastewater disinfection the time to a certain degree, thereby make water outlet reach the emission standard of " livestock and poultry breeding industry pollutant emission standard " regulation fully, both can safety dumping, can be back to the ground wash-down water in the pig house again.
In above-mentioned steps, biological concentration in the biological respinse storehouse cylindrical shell 1 will be controlled at 20000mg/L, and high biological concentration can guarantee biological respinse storehouse cylindrical shell, and (the pig farm sewage of chemical oxygen demand COD=5000～8000mg/L) has processing effect efficiently to high density; Described biologic packing material and iron plane flower mixture 16 is placed in the anaerobic hydrolysis storehouse and can forms the galvanic cell effect at 3 o'clock, thereby play the function of catalysis iron, the larger molecular organics that impels difficult degradation in the sewage more effectively issues unboiled water in the effect of anaerobe film 17 and separates, and forms the easily biochemical organism of small molecules; Described anaerobe film 17 is cultivated on conventional biologic packing material, and through the acting in conjunction of catalysis iron and anaerobe film 17, the biodegradability of residual COD is further improved in the sewage thereby make; In addition, iron plane flower and biologic packing material are to be that 0.5: 1 ratio is carried out blended according to volume ratio, can obviously strengthen the 3 pairs of organic destructions of complexity in anaerobic hydrolysis storehouse like this, improve the degradation effect in follow-up catalytic oxidation storehouse 4.
As depicted in figs. 1 and 2, in this specific embodiment, the integrated-type equipment that the present invention is used for above-mentioned scale pig farm sewage water treatment method comprises biological respinse storehouse cylindrical shell 1 (also can be described as MBR reaction warehouse cylindrical shell), membrane filtration storehouse 2, anaerobic hydrolysis storehouse 3, catalytic oxidation storehouse 4, sterilization storehouse 5 and equipment compartment 6.Biological respinse storehouse cylindrical shell 1 inner bottom part is equipped with some micro-hole aerator I7, and the top in the described biological respinse storehouse cylindrical shell 1 is equipped with some jet aerators 13, has two aerating systems thereby make in the biological respinse of the present invention storehouse cylindrical shell 1; Described some micro-hole aerator I 7 are interconnective by air line, and the required air of described micro-hole aerator I7 is by being arranged in the equipment compartment 5 and the gas blower 14 that is communicated with air line provides; Described biological respinse storehouse cylindrical shell 1 inwall is connected with two diaphragms 12; The top of described diaphragm 12 is lower than the elevation of water surface in the biological respinse storehouse cylindrical shell 1, and the bottom of described diaphragm 12 is higher than the bottom of biological respinse storehouse cylindrical shell 1, its objective is in order to guarantee that current can circulate up and down in the cylindrical shell of biological respinse storehouse; Described micro-hole aerator 7 is between two diaphragms 12.
In this specific embodiment, 2 middle parts, described membrane filtration storehouse directly are communicated with biological respinse storehouse cylindrical shell 1 by pipeline; 2 bottoms, described membrane filtration storehouse also are communicated with biological respinse storehouse cylindrical shell 1 by a water pump I8; Be provided with micro-filtration membrane module 9 in the described membrane filtration storehouse 2; Described water pump I8 is installed in the equipment compartment 6, and its effect is to impel active sludge and the larger molecular organics mass-energy held back by micro-filtration membrane module 9 enough to be back in the cylindrical shell of membrane biological reaction storehouse.Described micro-filtration membrane module 9 is communicated with anaerobic hydrolysis storehouse 3 by suction water pump 10, described micro-filtration membrane module 9 has the function that the membrane filtration water outlet is transported to the anaerobic hydrolysis storehouse under the effect of suction water pump 10, because micro-filtration membrane module 9 is a kind of prior aries, so do not give unnecessary details at this.
In this specific embodiment, described anaerobic hydrolysis storehouse 3 is communicated with catalytic oxidation storehouse 4 by pipeline; Described catalytic oxidation storehouse 4 is communicated with sterilization storehouse 5 by water pump II11; 4 bottoms, described catalytic oxidation storehouse are equipped with some micro-hole aerator II15, and described some micro-hole aerator II15 interconnect by air line; The required air of described micro-hole aerator II15 is by being arranged in the equipment compartment 6 and the gas blower 14 that is communicated with air line provides.Described water pump II11 and suction water pump 10 are installed in the equipment compartment 6; And the effect of water pump II11 is that the water in the catalytic oxidation storehouse 3 is transported in the sterilization storehouse 5.
Claims (7)
1, a kind of scale pig farm sewage water treatment method, it is characterized in that: it may further comprise the steps:
1., at first make sewage in biological respinse storehouse cylindrical shell (1), carry out biochemical reaction, and make the sewage behind the biochemical reaction flow in the membrane filtration storehouse (2) that directly is communicated with biological respinse storehouse cylindrical shell (1) by a pipeline;
2., utilize the micro-filtration membrane module (9) be installed in the membrane filtration storehouse (2) to hold back and flow through active sludge and larger molecular organics in the sewage that comes from biological respinse storehouse cylindrical shell (1), and make the membrane filtration water outlet by in the anaerobic hydrolysis storehouse (3) that suction water pump (10) flows into micro-filtration membrane module (9) is communicated with, make the sewage that has active sludge and larger molecular organics flow back to biological respinse storehouse cylindrical shell (1) by water pump I (8);
3., in anaerobic hydrolysis storehouse (3), the part macromole that is not degraded in the membrane filtration water outlet is hydrolyzed, the water outlet that biochemical obviously improves after the hydrolysis is flow in the catalytic oxidation storehouse (4) by pipeline;
4., in catalytic oxidation storehouse (4) to the further biodegrade of water outlet, make then water outlet pass through water pump II (11) flow into the sterilization storehouse in (5);
5., in sterilization storehouse (5), water outlet is decoloured and disinfect;
Wherein, the biological concentration in the described biological respinse storehouse cylindrical shell (1) is 19000mg/L～21000mg/L; Be provided with conventional biologic packing material in the described anaerobic hydrolysis storehouse (3), cultivating on the described conventional biologic packing material has anaerobe film (17); Be provided with floating stuffing (18) in the described catalytic oxidation storehouse (4), described floating stuffing (18) is gone up to cultivate aerobic biologic membrane (19); Be placed with sterilizing agent (20) in the described sterilization storehouse (5).
2, scale according to claim 1 pig farm sewage water treatment method is characterized in that: be placed with the iron plane flower in the described anaerobic hydrolysis storehouse (3); The volume ratio of described iron plane flower and biologic packing material is not higher than 0.5: 1.
3, scale according to claim 1 pig farm sewage water treatment method is characterized in that: the sterilizing agent (20) in the described sterilization storehouse (5) is a Losantin.
4, a kind of integrated-type equipment that is used for scale pig farm sewage water treatment method, it is characterized in that: it comprises biological respinse storehouse cylindrical shell (1), membrane filtration storehouse (2), anaerobic hydrolysis storehouse (3), catalytic oxidation storehouse (4), sterilization storehouse (5) and equipment compartment (6); Described biological respinse storehouse cylindrical shell (1) inner bottom part is equipped with some micro-hole aerator I (7); Described micro-hole aerator I (7) is used with gas blower (14); Middle part, described membrane filtration storehouse (2) directly is communicated with biological respinse storehouse cylindrical shell (1) by pipeline; Bottom, described membrane filtration storehouse (2) is communicated with biological respinse storehouse cylindrical shell (1) by a water pump I (8); Be provided with micro-filtration membrane module (9) in the described membrane filtration storehouse (2); Described micro-filtration membrane module (9) is communicated with anaerobic hydrolysis storehouse (3) by suction water pump (10); Described anaerobic hydrolysis storehouse (3) is communicated with catalytic oxidation storehouse (4) by pipeline; Described catalytic oxidation storehouse (4) is communicated with sterilization storehouse (5) by water pump II (11); Described gas blower (14), water pump I (8), water pump II (11) and suction water pump (10) are installed in the equipment compartment (6).
5, scale pig farm sewage integrated-type processing equipment according to claim 4, it is characterized in that: the top in the described biological respinse storehouse cylindrical shell (1) is equipped with some jet aerators (13).
6, scale pig farm sewage integrated-type processing equipment according to claim 5, it is characterized in that: described biological respinse storehouse cylindrical shell (1) inwall is connected with two diaphragms (12); The top of described diaphragm (12) is lower than the water level in the biological respinse storehouse cylindrical shell (1); The bottom of described diaphragm (12) is higher than the bottom of biological respinse storehouse cylindrical shell (1); Described micro-hole aerator (7) is positioned between two diaphragms (12).
7, scale pig farm sewage integrated-type processing equipment according to claim 4, it is characterized in that: bottom, described catalytic oxidation storehouse (4) is equipped with some micro-hole aerator II (15); Described micro-hole aerator II (15) is used with gas blower (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101200989A CN101323496B (en) | 2008-07-18 | 2008-07-18 | Scale hogpen sewage disposal method and integrated equipment thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2008101200989A CN101323496B (en) | 2008-07-18 | 2008-07-18 | Scale hogpen sewage disposal method and integrated equipment thereof |
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| Publication Number | Publication Date |
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| CN101323496A true CN101323496A (en) | 2008-12-17 |
| CN101323496B CN101323496B (en) | 2011-01-12 |
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| CN2008101200989A Expired - Fee Related CN101323496B (en) | 2008-07-18 | 2008-07-18 | Scale hogpen sewage disposal method and integrated equipment thereof |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105541003A (en) * | 2015-12-11 | 2016-05-04 | 青岛清科环保科技有限公司 | Method for treating aquaculture wastewater |
| CN106565058A (en) * | 2016-11-03 | 2017-04-19 | 聊城职业技术学院 | Stockyard sewage treatment technology |
| CN107281809A (en) * | 2017-06-30 | 2017-10-24 | 中山诺顿科研技术服务有限公司 | A kind of sewage filter device |
-
2008
- 2008-07-18 CN CN2008101200989A patent/CN101323496B/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105541003A (en) * | 2015-12-11 | 2016-05-04 | 青岛清科环保科技有限公司 | Method for treating aquaculture wastewater |
| CN106565058A (en) * | 2016-11-03 | 2017-04-19 | 聊城职业技术学院 | Stockyard sewage treatment technology |
| CN107281809A (en) * | 2017-06-30 | 2017-10-24 | 中山诺顿科研技术服务有限公司 | A kind of sewage filter device |
| CN107281809B (en) * | 2017-06-30 | 2019-12-10 | 江苏厚水环保技术有限公司 | sewage filtering device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN101323496B (en) | 2011-01-12 |
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