CN201882994U

CN201882994U - Environment-friendly organic sewage treatment device

Info

Publication number: CN201882994U
Application number: CN2010206297358U
Authority: CN
Inventors: 罗烈明; 罗逸
Original assignee: FANGMING ENVIRONMENTAL PROTECTION TECHNOLOGY (ZHANGZHOU) Co Ltd
Current assignee: Fujian Fangming Environmental Technology Co., Ltd.
Priority date: 2010-11-26
Filing date: 2010-11-26
Publication date: 2011-06-29
Anticipated expiration: 2020-11-26

Abstract

The utility model discloses an environment-friendly organic sewage treatment device, which comprises an electro-catalysis oxidation device and a precipitation device. The electro-catalysis oxidation device comprises an oxidation container and an electrode device mounted in the oxidation container, wherein the oxidation container is provided with a bottom water inlet and a top water outlet. The precipitation device comprises a precipitation container, a residue removal valve is arranged below the precipitation container, an adding device for adding chemical flocculating agent and a stirring device capable of stirring sewage are arranged on the precipitation container, and the precipitation container is provided with a bottom water inlet and a top water outlet. Besides, the water outlet of the oxidation container is communicated with the water inlet of the precipitation container. The environment-friendly organic sewage treatment device has the advantages of no secondary pollution and recycling of degraded sewage since harmful substance in sewage is oxidized by OH (hydroxide) ion generated by the electro-catalysis oxidation device, suspension is precipitated by the aid of the precipitation device and then the precipitation is treated.

Description

A kind of organic sewage environment-friendly processing unit

Technical field

The utility model relates to a kind of organic sewage environment-friendly processing unit.

Background technology

Organic sewage, for example pig industry sewage (being mainly derived from pig manure urine and food-residue that the flushing pigsty is taken out of), city domestic sewage are the treatment process of the existing organic sewage of example explanation and the technical problem that exists with pig industry sewage below.

In the modern pig industry; end user's construction method does not pick out before pig manure is rinsed, but adopts big water gaging process of washing that pig excrements is gone out pigsty in the lump, to improve the health clean level of pig house greatly; reduce growing of various germs significantly, reach the large-scale development of the intensive cultivation of pig.Because having mixed a high proportion of pig manure urine, these wash-down waters make objectionable impuritiess such as its chemical oxygen demand (COD) (COD), biological oxygen demand (BOD), ammonia nitrogen amount total phosphorus, intestinal bacteria, roundworm egg suspended substance seriously surpass the relevant emission standard of country, therefore generally exceed standard more than tens times, directly the discharging meeting has caused great destruction to environment.At present, because technical reason can only adopt following several method to handle above-mentioned wash-down water:

The one, biological process promptly produces wash-down water introduction methane-generating pit and discharges after biogas (recycling) is handled through aeration again through anaerobic treatment.There are following several defectives in this treatment process: the water after 1, handling can't be recycled, and directly discharging pollutes the environment; Though 2 biogas are handled back COD bigger reduction has been arranged, but when anerobe produces biogas at degradation of organic substances, can't decompose the objectionable impuritiess such as ammonia nitrogen total phosphorus in the sewage, make sewage ammonia nitrogen content superelevation, directly discharging easily makes the rivers body eutrophication, it is smelly to make algae and water grow water body, also can exceed standard because of not enough COD index of biogas reaction times simultaneously.The sewage of these eutrophication promptly is used in irrigation also can make plant morph because of ammonia nitrogen is too high or death; 3, can't eliminate germ and suspended substance in the sewage, the sewage overall performance still can't reach emission request; 4, biological process requires that all long biological decomposition time must be arranged, as anaerobism biogas genetic method general requirement main reaction pond more than 15 days, the aeration aerobic reaction is more than 30 days, precipitation clarification is more than 30 days about cumulative time 75-90 days, producing continuously under the situation of sewage, handle these sewage just need to build a large amount of these reaction tanks of reaction tank be day sewage quantity 75-90 doubly, not only construction investment huge, take a large amount of soils but also can't hide rainwater because of the pond is many and rainwater often takes place overflow the pollutent incident of bringing of releasing.

The 2nd, physico-chemical process promptly adopts methods such as solid-liquid separation, flocculation, coagulation to make the sewage flocculation precipitation, and taking out in the sewage has this material.There is following defective in this treatment process: facts have proved that 1, this method investment is big, and material consumption height, the cost of disposing of sewage reach more than 20 yuan/and per ton, and, also can't reach emission standard; 2, sewage residence time in treating processes long, the sewage lagoon capacity is big, generally is day more than the thirtyfold of sewage effluent amount, promptly needs great amount of investment, takies a large amount of soils again, brings very big burden to pig industry; 3, the reflection precision is difficult to control sewage in the application owing to generating after materialization is handled, can only adopt the excess reaction method that sewage is carried out physical reaction handles, react consequently that additive accumulates continuous increase and residual liquid that bigger cost of needs or trouble are handled additive, and the residue of reaction precipitation thing is difficult to utilize equally bring destruction to ecology again.

The utility model content

The utility model provides a kind of organic sewage environment-friendly processing unit, and it has overcome the existing deficiency of the sewage water treatment method in the background technology.

The technical scheme that is adopted that the utility model solves its technical problem is:

A kind of organic sewage environment-friendly processing unit, it comprises:

Electrocatalysis oxidation apparatus, it comprises that an oxidation container and is installed in the electrode device within the oxidation container, wherein, described oxidation container has the water outlet that a water-in and that is located at the bottom is located at the top;

Settler, it comprises a precipitation vessel, be provided with a scarfing cinder valve under the described precipitation vessel, be provided with the whipping appts that an adding set and that is used to add chemical floc can stir sewage on the described precipitation vessel, wherein, described precipitation vessel has the water outlet that a water-in and that is located at the bottom is located at the top;

The water outlet of described oxidation container is connected the water-in of precipitation vessel.

Among one preferred embodiment: described electrocatalysis oxidation apparatus is divided into first electrocatalysis oxidation apparatus and second electrocatalysis oxidation apparatus;

Described first electrocatalysis oxidation apparatus comprises that one first oxidation container and is installed in first electrode device within first oxidation container, described first electrode device such as comprises at number and even interval-staggered a plurality of positive electrodes and a plurality of negative potential, wherein, described first oxidation container has the water outlet that a water-in and that is located at the bottom is located at the top;

Described second electrocatalysis oxidation apparatus comprises that one second oxidation container and is installed in second electrode device within second oxidation container, add zeolite granular within described second oxidation container, described second electrode device such as comprises at number and even interval-staggered a plurality of positive electrodes and a plurality of negative potential, wherein, described second oxidation container has the water outlet that a water-in and that is located at the bottom is located at the top;

The water outlet of described first oxidation container is connected the water-in of second oxidation container, and the water outlet of described second oxidation container is connected the water-in of precipitation vessel.

The water outlet of described second oxidation container is connected the water-in of first oxidation container, and the water outlet of described first oxidation container is connected the water-in of precipitation vessel.

Among one preferred embodiment: it also comprises:

One supply unit, it comprises that a power supply and an electricity connect power supply and the supervisory control desk of the exchange positive and negative electrode that can circulate, electric respectively two electrodes that connect first electrode device of two electrodes of described supervisory control desk, electric respectively two electrodes that connect second electrode device of two electrodes of described supervisory control desk.

Among one preferred embodiment: it also comprises:

The electricity flocculation plant, it comprises that a flocculation container and is installed in the third electrode device within the flocculation container, described third electrode device comprises that two can conduct electricity the electrode basket that connects power positive cathode respectively, the material of described electrode basket adopts the insoluble petal material, described electrode basket offers mesh, be equiped with iron or aluminium electrode particle in the described electrode basket, wherein, described flocculation container has the water outlet that a water-in and that is located at the bottom is located at the top;

The water outlet of described flocculation container is connected the water-in of oxidation container.

Among one preferred embodiment: it also comprises:

The water outlet of described oxidation container is connected the water-in of flocculation container, and the water outlet of described flocculation container is connected the water-in of precipitation vessel.

Among one preferred embodiment: described settler comprises successively settling tank, precipitation vessel and settling pond side by side, all be provided with the scarfing cinder valve under described settling tank, precipitation vessel and the settling pond, described settling tank, precipitation vessel and settling pond all are provided with the spillway that a water-in and that is positioned at the bottom is located at the top; The water outlet of described second oxidation container is connected the water-in of settling tank, and the spillway of described settling tank is connected the water-in of precipitation vessel, and the spillway of described precipitation vessel is connected the water-in of settling pond.

Among one preferred embodiment: described settler comprises successively settling tank, precipitation vessel and settling pond side by side, all be provided with the scarfing cinder valve under described settling tank, precipitation vessel and the settling pond, described settling tank, precipitation vessel and settling pond all are provided with the spillway that a water-in and that is positioned at the bottom is located at the top; The water outlet of described first oxidation container is connected the water-in of settling tank, and the spillway of described settling tank is connected the water-in of precipitation vessel, and the spillway of described precipitation vessel is connected the water-in of settling pond.

Among one preferred embodiment: an adsorption unit, it comprises the contactor that flyash is housed in, it connects the scarfing cinder valve.

The technical program is compared with background technology, and it has following advantage:

1, produces objectionable impurities in the OH ionic oxide formation sewage by electrocatalysis oxidation apparatus, handle throw out again, therefore can overcome the existing deficiency of background technology, and have following advantage: a. and control simply by settler precipitation suspended substance; B. safeguard easily; C. non-secondary pollution; D. residue is few and can directly utilize; E. the recyclable utilization of degraded back sewage; G. the occupation of land of environment-friendly processing unit compact construction is few, and dismounting can realize resettlement easily, can not waste; H. realize the continuous degradation of sewage, sewage quantity can be monitored, and the sewage disposal index is adjustable, but the management and control of sewage disposal working hour had so not only helped applying unit and made things convenient for use and management but also be beneficial to environmental administration's supervision; I. lower, the low equipment investment of the unit cost of degradation of sewage, scientific research is extensively accepted by the user; Save water resources and prevented the water pollution;

2, not only can produce objectionable impurities in the flocculation agent flocculation treatment sewage by electric flocculation plant, and can also electrolysis go out the objectionable impurities in the OH ionic oxide formation sewage;

3, by flyash adsorption precipitation thing, can be after the drying directly as organic fertilizer;

4, add zeolite granular in second oxidation container of second electrocatalysis oxidation apparatus, this zeolite particles can be improved the soil, and, itself is insoluble to sewage, only in electrochemical reaction process, play and convert H ion and O ion to have OH hydroxyl radical free radical ionic effect than the strong oxidizing property energy, itself can also adsorb ammonia nitrogen and phosphorus suspended substance in the sewage, adsorbing competent ammonia nitrogen material can be directly as the nitrogenous fertilizer effect, the discarded back of this zeolite particles non-secondary pollution.

Description of drawings

The utility model is described in further detail below in conjunction with drawings and Examples.

Fig. 1 has illustrated the synoptic diagram of the organic sewage environment-friendly processing unit of first preferred embodiment.

Fig. 2 has illustrated the synoptic diagram of first electrocatalysis oxidation apparatus of first preferred embodiment.

Fig. 3 has illustrated the synoptic diagram of second electrocatalysis oxidation apparatus of first preferred embodiment.

Fig. 4 has illustrated the synoptic diagram of the electric flocculation plant of first preferred embodiment.

Fig. 5 has illustrated the synoptic diagram of first electrocatalysis oxidation apparatus of second preferred embodiment

Fig. 6 has illustrated the B place enlarged diagram of Fig. 5.

Fig. 7 has illustrated the synoptic diagram of combinations such as positive conducting rod, positive electrode.

Fig. 8 has illustrated the synoptic diagram of the organic sewage environment-friendly processing unit of the 4th preferred embodiment.

Embodiment

First preferred embodiment

Please refer to Fig. 1, a kind of organic sewage environment-friendly processing unit, it comprises at least one electrocatalysis oxidation apparatus, at least one electric flocculation plant 300, a supply unit and a settler.Among the present embodiment, described electrocatalysis oxidation apparatus number is not limit, according to sewage content of harmful decision, following embodiment and accompanying drawing be with two be example, these two are defined as first electrocatalysis oxidation apparatus 100 and second electrocatalysis oxidation apparatus 200 respectively.As required, also applicable three or more, for example two first electrocatalysis oxidation apparatus 100 and one second electrocatalysis oxidation apparatus 200, perhaps, one first electrocatalysis oxidation apparatus 100 and two second electrocatalysis oxidation apparatus 200.

Among the present embodiment, the sewage disposal of described electrocatalysis oxidation apparatus and electric flocculation plant 300 flows to and does not limit, electrocatalysis oxidation apparatus can be positioned at before the electric flocculation plant 300, also can be positioned at after the electric flocculation plant 300, first electrocatalysis oxidation apparatus 100 can be positioned at before second electrocatalysis oxidation apparatus 200, also can be positioned at after second electrocatalysis oxidation apparatus 200.Among the present embodiment, sewage disposal flows to and is: first electrocatalysis oxidation apparatus 100 ... second electrocatalysis oxidation apparatus 200 ... electricity flocculation plant 300.Described first electrocatalysis oxidation apparatus 100 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, described second electrocatalysis oxidation apparatus 200 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, and described electric flocculation plant 300 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top.First electrocatalysis oxidation apparatus, 100 water-ins insert sewage, the water-in of described second electrocatalysis oxidation apparatus 200 is connected the water outlet of first electrocatalysis oxidation apparatus 100, and the water-in of described electric flocculation plant 300 is connected the water outlet of second electrocatalysis oxidation apparatus 200.The water outlet of described electric flocculation plant 300 is connected the water inlet of settler.Best, be provided with a under meter and valve to be opened/closed at the water inlet place of first electrocatalysis oxidation apparatus 100.Under meter is used to monitor sewage load, closes sewage when valve is used for equipment repair and maintenance and enters.

Described first electrocatalysis oxidation apparatus 100, comprise that one first oxidation container and is installed in first electrode device within first oxidation container, described first electrode device obtains electric energy, then can electrolysis separate out the OH ion from sewage, described OH ion can be degraded into oxidation operation in the sewage can evaporable CO ₂And N ₂, concrete structure is asked for an interview and is described below.

Described second electrocatalysis oxidation apparatus 200, comprise that one second oxidation container and is installed in second electrode device within second oxidation container, and, adding zeolite granular as third electrode in the sewage of described second oxidation container, concrete structure is asked for an interview and is described below.The positive and negative electrode of second electrode device obtains electric energy, then decomposite H ion and O ion in the sewage liquid, then zeolite granular can form small galvanic cell, small galvanic cell converts H ion and O ion to OH hydroxyl radical free radical ion, reach strong oxidation effectiveness, be particularly useful for containing the sewage degraded of high ammonia nitrogen of difficult degradation and high COD; The positive and negative electrode of second electrode device obtains electric energy, and zeolite granular plays the granule electrode effect and brings into play the ion transformation and makes a large amount of OH hydroxyl radical free radical ion of generation in electrode weekly form and the liquid; And described zeolite granular has the effectiveness above the strong degradation of ammonia nitrogen of carbon class particle, and the discarded back of this zeolite particles non-secondary pollution can directly use as nitrogenous fertilizer after having adsorbed competent ammonia nitrogen material in this zeolite particles.

Described electric flocculation plant 300, it comprises that a flocculation container and is installed in the third electrode device within the flocculation container, described third electrode device obtains electric energy, then can from sewage, electrolysis separate out the OH ion, the electrode ion is separated out in electrolysis, and described electrode ion and OH ion can be combined to flocculation agent, and described flocculation agent flocculates into wadding with sewage generation flocculation reaction with objectionable impurities in the sewage (as total phosphorus, suspended substance etc.), and then precipitation, concrete structure is asked for an interview and is described below.Electrode ion among the present embodiment can be electrode particle and separates out formation, the optional iron particle of described electrode particle also optional aluminum particulate through electrolysis.

Described supply unit comprises a power supply 420 and a supervisory control desk 410, described power supply 420 optional generators, store battery, direct external civil power etc.Described power supply 420 connects supervisory control desks 410, described supervisory control desk 410 conductions connect first, second, the positive and negative electrode of second electrode device, and can make positive and negative electrode circulation exchange.Among the present embodiment, power supply and supervisory control desk, this supervisory control desk are provided with rectifier power source can be rectified into direct current and controllable adjustable with the electrical network electricity (380V) of input.Power supply is provided with two utmost points, positive pole and negative poles of output DC.Two polarity can be exchanged automatically, and the pitch time of exchange and working hour can be provided with and regulate, reciprocal time and working hour can be provided with and adjusting, reciprocal time and working hour scope by 1 second to 1 hour.This electric power outputting current and voltage range 1A-5 ten thousand A, voltage 1V-110V.Set according to the sewage quantity that need are handled.This power supply can output DC or the output pulse direct current, and can establish the press button of power switch, instrument, earth leakage circuit-breaker, air switch, open-phase protection switch and control device work.Described first, second, second electrode device and supervisory control desk, power supply can be with being connected in parallel, also can be with being connected in series, present case adopts and is connected in series to reach energy-saving effect.

Described settler, it comprises successively side by side at least one settling tank 510, at least one precipitation vessel 520 and at least one settling pond 530, all is provided with the scarfing cinder valve under described settling tank 510, precipitation vessel 520 and the settling pond 530.Described settling tank 510 connects the water outlet of electric flocculation plant 400, the spillway of described settling tank 510 is arranged on the top and connects precipitation vessel 520, the spillway of described precipitation vessel 520 is arranged on the top and connects settling pond 530, and the spillway of described settling pond 530 can be discharged the liquid after handling.Among the present embodiment, described precipitation vessel 520 is provided with the whipping appts that an adding set and that is used to add chemical floc can stir sewage.Described flocculation agent for example is poly-ferric chloride, polymerize aluminum chloride etc.Best, establish a transparent windows at the spillway of settling pond 530 and be used to observe delivery turbidity.

As required, also can press from both sides and establish an adsorption unit 600, in the described adsorption unit 600 flyash is housed, be used to adsorb the throw out of discharging by the scarfing cinder valve, after drying can be directly as organic fertilizer.

Among the present embodiment, the sheating material of described electrocatalysis oxidation apparatus, electric flocculation plant 300 and settler all adopts the steel or stainless steel material, and last goods and materials can all be recycled and promptly not have the recoverable again part cost of investment of waste, non-secondary pollution after then scrapping.

Please refer to Fig. 2, described first electrocatalysis oxidation apparatus 100, it comprises that one first oxidation container 110 and is installed in first electrode device 120 within first oxidation container 110.Described first oxidation container 110 comprises a shell and is located at the insulation inwall of shell internal perisporium that the medial surface of described insulation inwall is an inner cylinder.Described first oxidation container 110 offers water-in that is positioned at first oxidation container, 110 bottoms and the water outlet that is positioned at the first oxidation container top, sewage charges within first oxidation container 110 by water-in, and the sewage after the processing enters next device by water outlet.Described first electrode device 120 is installed within first oxidation container 110, and comprises positive conducting plates 121, one a negative conducting plates 122, some positive electrodes 123, some negative potentials 124 at least.Described positive conducting plates 121 has one first side; Those positive electrodes 123 evenly conduct electricity at interval and are fixed in positive conducting plates 121 first sides; Described negative conducting plates 122 has one second side; Those negative potentials 124 evenly conduct electricity at interval and are fixed in negative conducting plates 122 second sides; Described positive conducting plates 121 and negative conducting plates 122 be towards layout, first side and second side towards, and those positive electrodes 123 and those negative potentials 124 are staggered and evenly at interval.Described first electrode device 120 obtains electric energy, then can electrolysis separate out the OH ion from sewage, and described OH ion can be degraded into oxidation operation in the sewage can evaporable CO ₂And N ₂Connect a plurality of positive electrodes 123 by positive conducting plates 121, connect a plurality of negative potentials 124 by negative conducting plates 122, described positive and negative electrode is staggered evenly to be arranged at interval, then interelectrode distance is little, electrode area is big in the volume, structure is compact, firmly, be convenient to safeguard, then conduct electricity very well, catalytic oxidation is effective, is particularly useful in the sewage degradation process.

Among the present embodiment, best, described positive conducting plates 121 and negative conducting plates 122 all are arc-like sheet, and described first side is the intrados of positive conducting plates 121, and described second side is the intrados of negative conducting plates 122.Because positive conducting plates 121 and negative conducting plates 122 all are arc-like sheet, therefore to be convenient to install, the electric field performance is good.

Among the present embodiment, best, described positive and negative electrode 123,124 thickness all are 0.1-5mm, optional 3mm, and the spacing between every adjacent two positive electrodes 123 is 6mm, spacing between every adjacent two negative potentials 124 is 6mm, and the spacing between every adjacent positive and negative electrode 121,122 is 3mm.

Among the present embodiment, best, described positive conducting plates 121 and negative conducting plates 122 are installed within the insulation inwall of shell, leave the gap between described insulation inwall and the positive and negative conducting plates 121,122.Because perisporium is provided with the insulation inwall within the shell, leave the gap between insulation inwall and the positive and negative conducting plates, therefore can prevent electric leakage, saves energy, the electric field performance is good.

Among the present embodiment, best, it also comprises one first fixed link 125, and it has insulating property, and its material can adopt nylon.Described first fixed link 125 is arranged to bolt arrangement, and vertically pass those positive and negative electrodes 123,124, and, all be provided with first insulating mat between every adjacent positive and negative electrode 123,124, described first insulating mat is socketed on first fixed link 125, other sets insulation nut 128 first fixed link 125 that is spirally connected, so that those positive and negative electrodes 123,124, first insulating mat are fixed together.Other establishes and sets up fixed link, not only can fixedly positioning electrode, and the positive and negative electrode that can also insulate.

Among the present embodiment, best, it also comprises 2 second fixed links 126, and it has insulating property, and its material can adopt nylon.This 2 second fixed link 126 vertically passes those positive and negative electrodes 123,124 and it is fixed together with those positive and negative electrodes 123,124, and, all be provided with second insulating mat between every adjacent positive and negative electrode 123,124, described second insulating mat is socketed on second fixed link 126.Other establishes and sets up fixed link, not only can fixedly positioning electrode, and the positive and negative electrode that can also insulate.

Among the present embodiment, best, cambered surface connects busbar 127 outside just being provided with outside the described positive conducting plates 121, and cambered surface is provided with the negative outer busbar 129 that connects outside the described negative conducting plates 122.The described positive and negative busbar 127,129 that connects conduct electricity two electrodes of supervisory control desk 410 of connection supply unit respectively.

Among the present embodiment, best, positive and negative electrode 123,124 configurations of surface are uneven surface; Best, the positive and negative electrode material can be selected for use and be the insoluble petal material, or, be insoluble petal base material top layer oxide covering material (DSA electrode); Best, positive and negative electrode area ratio is 1: 1.

Please refer to Fig. 3, described second electrocatalysis oxidation apparatus 200 comprises one second oxidation container 210, is equiped with at least one second electrode device 220 within described second oxidation container 210.Described second electrode device 220 such as comprises at number and even interval-staggered a plurality of positive electrodes and a plurality of negative potential, adds zeolite granular in the liquid within the described container to be used for as third electrode, to constitute the three-diemsnional electrode device.

Among the present embodiment, best, the structure of described second electrode device 220 is with reference to the structure of first electrode device 120.Among the present embodiment, not having under the situation of liquid, is mutual nonconducting trip condition between positive and negative two electrodes.Two electrodes of described second electrode device 220 connect two electrodes of the supervisory control desk of supply unit respectively.Among the present embodiment, best, the positive and negative electrode configuration of surface of second electrode device 220 is a uneven surface; Best, the positive and negative electrode material can be selected for use and be the insoluble petal material, or, be insoluble petal base material top layer oxide covering material (DSA electrode); Best, positive and negative electrode area ratio is 1: 1.

Among the present embodiment, can only establish one second electrode device 220, a plurality of second electrode devicies 220 also can be set.If a plurality of, then preferably those second electrode devicies 220 between the upper and lower every setting, and be advisable can all being immersed in the liquid (the neighbouring two electrode group alternate directions of present case are arranged).Among the present embodiment, second electrode device, 220 arrangement pitches are greater than 0 and less than 10cm between layer and the layer, and present case preferred plan is 10cm, 15cm, 20cm.Up and down between second electrode device 220 except that the conducting wire is communicated with, do not having under the liquid situation, not conducting of electric current is in off-state.

Among the present embodiment, best, the water inlet of described second oxidation container 210 is positioned at the bottom, and water outlet is positioned at the top, and described water inlet is connected the water outlet of first oxidation container 110, and described water outlet is discharged treated sewage.

Among the present embodiment, best, described second oxidation container 210 comprises that a shell, is located at insulation inwall and within the shell and can installs and removes lid and be connected on lid 230 on the shell.Best, described shell can adopt stainless steel, steel, glass reinforced plastic, plastics or titanium alloy etc materials to make according to the corrodibility degree of sewage.Best, described lid is provided with an air outlet, is used to volatilize discharge the gas of degraded, and place, described air outlet is connected with an anti-foam and overflows net, is used to prevent that the sewage foam from overflowing outside second oxidation container.

Among the present embodiment, best, the bottom of described second oxidation container 210 is provided with a Butterworth Hatch, described Butterworth Hatch place is equiped with one and cleans dirt valve 240, when being used for the components and parts in clean container, liquid after the cleaning can be discharged by cleaning dirt valve 240, and the slag body that cleans out can adsorb direct as fertilizer sources by flyash to be used.

Among the present embodiment, best, also establish at least one cycling mechanism on described second oxidation container 210, it comprises that one is installed in the recycle pump 250 and a circulation tube 260 of the lid 230 of second oxidation container 210, described circulation tube 260 1 ends are connected a circulation port that is opened in second oxidation container, 210 bottoms, the other end is connected second oxidation container, 210 tops, described recycle pump 250 connects circulation tube 260, the water of second oxidation container, 210 bottoms can be evacuated to the top and dash downwards, by the liquid in the abundant circulation stirred vessel under the liquid, so that the three-diemsnional electrode particle evenly is suspended in liquid.

Among the present embodiment, best, the place, bottom of described second oxidation container 210 is provided with a cushioning pocket layer 270.

Among the present embodiment, insulate with insulation compound or wrapping insulation layer method in non-conductive contact position.

Among the present embodiment, the amount that adds zeolite granular is the 1-20% of liquid weight, and this scope contains the ammonia nitrogen amount according to sewage and decides, and will lack when sewage contains the ammonia nitrogen amount hour number of particles of filling out, and is also many when big.Among the present embodiment, zeolite granular can be selected natural zeolite or synthetic zeolite for use, and its particle size range is greater than 30 orders and less than 1mm.Particle size range decides according to electrode group current density size, and particle diameter was also big when current density was big, and current density hour particle diameter is also little.Present case is selected 0.1A/dm ²The corresponding 30 order particle diameter zeolites of electric current, 0.5A/dm ²The time corresponding 20 orders, 1A/dm ²The time corresponding 0.1mm particle diameter, 1.5A/dm ²The time corresponding 0.5mm particle diameter, 2A/dm ²The time corresponding 0.8mm particle diameter, 3A/dm ²The time corresponding 1mm particle diameter.

Among the present embodiment, the following description of sewage degradation process: sewage enters within second oxidation container 210 by water inlet, through the three-diemsnional electrode device reaction sewage is degraded to gas N ₂, CO ₂With processing back liquid, handle back liquid and discharge by water outlet.Among the present embodiment, handle following description: positive and negative electrode obtains electric energy, then decomposites H ion and O ion in the sewage liquid, and then zeolite granular can form small galvanic cell, small galvanic cell converts H ion and O ion to OH hydroxyl radical free radical ion, reaches strong oxidation effectiveness; Positive and negative electrode obtains electric energy, and zeolite granular plays the granule electrode effect and brings into play the ion transformation and makes a large amount of OH hydroxyl radical free radical ion of generation in electrode weekly form and the liquid.Among the present embodiment, adopt the zeolite particles particle as the three-diemsnional electrode particle, effectiveness with the strong degradation of ammonia nitrogen that surpasses carbon class particle, and, the discarded back of this zeolite particles non-secondary pollution, can directly use as nitrogenous fertilizer behind the competent ammonia nitrogen material of absorption in this zeolite particles, this zeolite particles can adopt the also applicable synthetic zeolite powder of natural zeolite powder.

Please refer to Fig. 4, described electric flocculation plant 300, it comprises flocculation container 310 and third electrode device 320.

Described flocculation container 310 is used to adorn sewage liquid, and it comprises that a shell and can install and remove lid and be connected on cover on the shell.The insulation inwall fixedly has been sticked within the described shell.Described sheating material adopts ageing-resistant corrosion-resistant material, among the present embodiment, can adopt steel, stainless steel, glass reinforced plastic or plastics etc.Described shell shape is not limit, and for example can adopt prismatic or cylindrical or inverted triangle doline or terrace with edge shape or pyramid etc.Among the present embodiment, internal space, described flocculation container 310 bottom up big and down small and its big or smallly dwindle similar taper or frustum with direct ratio.Be installed with bracing frame 340 on described flocculation container 310 bottom centre, be used to make described flocculation container 310 bottoms to form slag funnel 350.

Among the present embodiment, best, described flocculation container 310 offers the water outlet that a water inlet and that is positioned at the bottom is positioned at the top.Described water inlet place is connected with a sewage water inlet pipe, then can charge within the flocculation container 310 through the sewage that second electrocatalysis oxidation apparatus 200 is handled by sewage water inlet pipe.Can discharge the liquid of flocculation reaction by water outlet.As required, also can establish the natural overflow port of sewage in flocculation container 310 upper ends.

Among the present embodiment, best, offer venting port on the cover of described flocculation container 310, be used for the volatile gases that the sewage effluent liquid degradation generates or separates out, as N ₂Gas; Best, described exhaust ports connects anti-foam and overflows net, is used to prevent take out of when gas from overflowing foam.

Among the present embodiment, best, the bottom of described flocculation container 310 is provided with the valve 360 of slagging tap, and is used for granulated slag or slag particle that the flocculation of effluent sewerage liquid degradation generates.Among the present embodiment, this valve 360 is as far as possible big under bottom size permission situation, is convenient to granulated slag or slag particle is arranged clearly, and, after this valve 360 is closed, liquid mouthful outflow from then on.

Among the present embodiment, best, described third electrode device 320 comprises two electrode baskets 321 independently, and described electrode basket 321 materials adopt insoluble petal material, for example titanium metal or stainless steel metal.All be equiped with electrode particle in the described two electrode baskets 321, described electrode particle is meant and can be electrolyzed to produce the electrode ionic, and described electrode ion and OH ion combination can become the particle of flocculation agent.Among the present embodiment, two electrode baskets conduct electricity two electrodes that connect supervisory control desk respectively.Among the present embodiment, the described two electrode baskets layout of being separated by.Among the present embodiment, the electrode basket adopts insoluble material to make, in the electrode basket electrode particle is housed, then avoided the electrode basket of electrode effect to be dissolved by electrolysis, need not to change the electrode basket in the reaction process, only need according to electrolytic speed loading electrode particle in the electrode basket, can guarantee that electrolysis continues to carry out, then electrode particle can adopt the waste and old iron that do not contain nuisance or aluminum metallic material to chop up to make, then interelectrode distance keeps in the electrolysis process of not stopping always, then the electrode basket is made simple, cheap, then interpolation or replacing electrode particle are simple to operation, guarantee that then electrode particle can be electrolyzed to produce the electrode ion, then can solve direct employing electrode particle material and make the electrode basket and existing deficiency: a. electrode is under the conduction working condition, under certain area condition, electrode materials purity homogeneity and current density microinhomogeneity all are inevitable, so the solution plane of electrode (anode) can produce inhomogeneous situation, this inhomogeneous meeting causes interelectrode distance to enlarge variation, can strengthen power consumption; B. under the bigger situation of electrode area, carry out manual method, automated method and all be difficult to reach the ideal adjustment, and the shaped electrode cost of manufacture is also higher, can not reach economic and practical purpose, therefore be difficult to enter in the production application.

Among the present embodiment, best, described electrode basket 321 comprises the component wall of slag tap wall 3212 and double-plate that a work wall 3211, of vertically arranging is in tilted layout, a described component wall is fixed in limit, work wall 3211 left side and the limit, wall 3212 left side of slagging tap, another component wall is fixed in work wall 3211 right edge and wall 3212 right edge of slagging tap, and make described electrode basket 321 internal spaces up big and down small, make electrode particle slide naturally under the natural gravity effect and under the inclination squeezing action of wall 3212 of slagging tap and be extruded into the heap shape downwards.

Among the present embodiment, best, the bottom of described electrode basket 321 can be connected with a diapire, as shown in Figure 4, but not as limit, described work wall 3211 bases and slag tap wall 3212 bases also can be directly affixed.As required, be connected with a roof on described work wall 3211, slag tap wall 3212, the component wall.

Among the present embodiment, best, the medial surface of each wall of described electrode basket 321 preferably all adds the reinforcement gusset, is used to gain in strength, and increases conductive area.Among the present embodiment, described electrode basket 321 sizes are calculated definite according to the consumption of electrode speed of electrode particle and the filler time of at interval additional electrode particle.Among the present embodiment, described structure body wall can play auxiliary effect with electrode particle in the electric current iontophoresis electrode basket 321.

Among the present embodiment, best, the described work wall 3211 and the wall 3212 of slagging tap all are provided with mesh, and the mesh bore of described work wall 3211 is less than the mesh bore of the wall 3212 of slagging tap.Among the present embodiment, best, described mesh for example is a tetragon, and described bore is meant tetragonal diagonal distance, and described mesh for example is circular, and described bore is meant diameter, and described mesh for example is a sexangle, and described bore is meant 2 times of length of sides.Among the present embodiment, described work wall 3211 mesh bores are elected 1-3mm as, and the described wall 3212 mesh bores of slagging tap are elected 2-5mm as.

Among the present embodiment, best, leave the gap between described electrode basket 321 and the insulation inwall 111, described two electrode baskets, 321 symmetric arrangement, described two work walls, 3211 parallel surfaces are to arranging at interval, described two work walls, 3211 spacings are greater than zero and non-conductive, and among the present embodiment, described spacing is selected 1-5mm for use.

Among the present embodiment, best, described two electrode baskets, 321 bottom supports and are provided with insulating mat between them on the bracing frame 340 of flocculation container 310, and described two electrode baskets 321 are positioned within the flocculation container 310.

Among the present embodiment, the material of described electrode particle adopts iron or aluminium, determine to adopt iron or aluminum according to the character of sewage or flocculating effect or sedimentary purposes, wherein: adopt that iron material has that higher oxygen evolution potential, price are low, obtain the advantage that liquid can utilize again behind the non-secondary pollution, flocculation, adopt aluminum to have the advantage that electric flocculating effect is good, the secondary pollution degree is little.Among the present embodiment, best, described iron particle can adopt shapes such as slice.This granular size so that manually add and chop up be made as suitable.The particle shape of this adding is not limit, but particle footpath size is greater than the electrode basket wall mesh bore of slagging tap, and (present case is selected 10-50mm for use) is used to avoid particle to pass the electrode basket by mesh.

Among the present embodiment, best, by busbar 370 electrolysis supervisory control desks, and pass cover toward in, and its positive and negative electrode conducts electricity the component wall that connects two electrode baskets 321 respectively from outer, make described two electrode baskets 321 conduct electricity company's positive and negative electrode respectively.Among this enforcement, described busbar is invaded liquid portion and is had limit all round, wherein closely is connected to rise with electrode basket component wall on one side to import a galvanic action, in addition two limits expose (limit that exposes must insulate prevent the dissolving of busbar and consume influence conductive effect).

Among the present embodiment, described two electrode baskets 321 obtain electric energy, then the OH ion is separated out in electrolysis in the sewage liquid, described electrode particle electrolysis is formed the electrode ion, described OH ion and electrode ionization synthetic flocculant (ironic hydroxide or aluminium hydroxide), described flocculation agent flocculates into wadding with the generation flocculation reaction of sewage liquid with objectionable impurities in the sewage liquid, thus volume is swept nuisance in the sewage, and the part nuisance is separated with sewage through precipitation, in order to handling.Described OH ion has oxidation effectiveness, the objectionable impurities in also can degradation of sewage.When the iron particle along with electrolytic reaction diminishes gradually, little of when slagging tap wall mesh bore, because of the mesh of natural gravity effect from the wall of slagging tap drops out, fall on the slag funnel, this slag can not extruded from work wall mesh (because work wall mesh is less than the wall mesh of slagging tap, if there are indivedual wedge angles to protrude from mesh, also can concentrate principle to parse rapidly because of current density is most advanced and sophisticated, can not cause because of the tip protrusion short circuit current phenomenon taking place).Electrode particle consumes along with carrying out continuously of electrolytic reaction and diminishes, naturally sliding downwards under the natural gravity effect and under the inclination squeezing action of wall 3212 of slagging tap and be extruded into the heap shape, conducting electric current and can bear bigger current density mutually then, can increase surface-area again and can bring into play the electrolysis advantage, thereby then simultaneously make the little response voltage saves energy consumption to greatest extent that reduces of trying one's best of two electrode baskets, 321 spacings because of the effect of being close to and rely on electrode basket 321 to work walls 3211.

Among the present embodiment, best, the exchange that can circulate of the positive and negative electrode of described two electrode baskets 321 dissolves the suspended substance of electrode surface absorption can make the positive and negative electrode cycle alternation, can make electrode conductivuty lasting, has also played effect for prolonging the time of replenishing electrode particle.

For the ease of in electrode basket 321, adding electrode particle, on described cover, offer two feed inlets 380, described two feed inlets 380 places all are connected with a lid door that can open or close, and described feed inlet 380 extends downwards.Offer the opening of corresponding feed inlet 380 on the roof of described electrode basket 321.Described two feed inlets, the 380 place adaptive respectively opening that puts in the roof of two electrode baskets 321 in bottom.Then the user opens after the lid door, can install electrode particle additional within two electrode baskets 321 by feed inlet 121.Among the present embodiment, described feed inlet 380 preferably is inverted ladder-shaped body, this feed inlet suitable for reading bigger than end opening, then can produce following advantage: 1. the electrode particle of being convenient to suitable for reading adds, the end opening width is slightly larger than extreme electrode particulate size, can prevent that then particle that size exceeds standard from inserting and cause faults such as particle is stuck; 2. upper and lower opening length is identical with the roof length of electrode basket, be to prevent from that the electrode particle that adds is deposited in to be the mountain shape under the feed inlet and to pile up and influenced electrode basket work wall area when adding electrode particle, can establish in addition and can stretch into club, to move flat its accumulation whole by feed inlet 380.

Along with the carrying out of electrolytic reaction, electrode particle diminishes the effect that is subjected to natural gravity gradually and descends gradually in the electrolytic reaction process.Because it is in the closed reactor, be the convenient position of observing electrode particle, establish one with the vertical marking component 330 of horizontal direction.Described marking component 330 can slide up and down and be connected flocculation container 310, it comprises that a sinker 331 and is fixed in the sign bar 332 on the sinker 331, among the present embodiment, the area of described sinker 331 is greater than the iron particle, described sinker 331 is put within the electrode basket 321 from top to down, and stretch out outside the lid of flocculation container 310 described sign bar 332 upper ends.Best, establish scale on the described sign bar 332, described scale is with to indicate bar 332 height of living in suitable, and is suitable with iron particulate within the electrode basket 321 sum that takes up room, so that reading.Wherein: these sign bar 332 length preferably surpass on one of the electrode basket 321 work walls 3211 length false add stretches out reactor cover sum, this sinker 331 is gone to the bottom planomural more preferably greater than electrode particle more than 3 times, less than electrode basket 321 work walls 3,211 1/2nd, can diminish with separating out of electrode particle so that indicate bar, surface location descends and descends and play the effect that indicates electrode particle upper surface position.

Among the present embodiment, the offering the corresponding bracing frame in position and make the roughly flow direction of the sewage liquid that enters be of the sewage water inlet of best described container: outside two electrode basket 321 cracks, work wall, electrode basket internal space, the wall of slagging tap, the electrode basket, thereby increase the electrolysis degree of sewage liquid.

Be referred to as slag from the electrode basket 321 electrode small-particle that wall 3212 falls down of slagging tap, this slag falls down the back from the wall of slagging tap and is deposited in naturally on the slag funnel 350; The throw out of flocculation is deposited on the slag funnel 350 naturally.The volume of described slag funnel 350 can be determined according to scarfing cinder pitch time as calculated.By valve 360 scarfing cinders of slagging tap, the small electrode particle in the scarfing cinder can utilize again during scarfing cinder.Its utilize as: from the small electrode particle that slag removing hole is discharged, can melt down dissolving after drying and make the standard electrode particle again and utilize again, also can directly directly recycle, can not constitute secondary pollution, can offset a part of cost when waste metal.

A kind of organic sewage environment-friendly treatment method, it comprises:

Step 10, electrode catalytic oxidation step is separated out the OH ion by electrolysis process, and described OH ion is degraded into oxidation operation in the sewage can evaporable CO ₂And N ₂

Step 20, electric flocculation step is separated out electrode ion and OH ion by the electrolysis process electrolysis, and flocculation agent is synthesized in described electrode ion and OH ionization, and described flocculation agent flocculates into wadding with sewage generation flocculation reaction with objectionable impurities in the sewage, and then precipitation.

Step 30, settling step adds chemical floc, and described flocculation agent flocculates into wadding with sewage generation flocculation reaction with objectionable impurities in the sewage, and then precipitation.

Step 40, adsorption step is used for the throw out by flyash adsorption step 30, and is dry again with as organic fertilizer.

Among the present embodiment, described step 20, it comprises:

Step 21, two electrode baskets 321 of described third electrode device 320 obtain electric energy, and the sewage liquid electrolytic in the flocculation container 310 is separated out the OH ion, and the electrode particle electrolysis in the electrode basket 321 is generated the electrode ion;

Step 22, described OH ion and electrode ionization synthetic flocculant;

Step 23, described flocculation agent flocculates into wadding with the generation flocculation reaction of sewage liquid with objectionable impurities in the sewage liquid, and then precipitation is in order to handling.

Best: as before step 10, also to include step 0, be used for adding sodium chloride solution toward sewage; Perhaps, in above-mentioned steps 10, step 20, all slowly add sodium chloride solution by volumetry.

Be added with NaCl solution, then produce a large amount of HOCL in electrode weekly form and the liquid ₂Ion, HOCL ₂Ion generation strong oxidation and germ killing action, thus degraded the organism in the sewage and other objectionable impurities.In liquid, add NaCl solution, in electrode catalytic oxidation process, can reduce the reaction power consumption, can in electrode weekly form and liquid, produce HOCL again ₂Ion, HOCL ₂Ion generation strong oxidation and germ killing action, thus degraded the organism in the sewage and other objectionable impurities.Among the present embodiment, the described strength of fluid that is added with NaCl solution and can be regulated concentration according to the content of harmful germ of interior degradation of sewage in the 0-5g/L scope.

Second preferred embodiment

This preferred embodiment and embodiment one difference are: please refer to Fig. 5, Fig. 6, Fig. 7, described first electrode device 120 ' comprise a positive conducting rod 121 ', a negative conducting rod 122 ', some positive electrodes 123 ', with the positive mandrin 125 ' of number such as positive electrode, with the negative potential 124 ' of number such as positive electrode and the negative mandrin 126 ' counted with negative potential etc.; Described each positive and negative electrode 123 ', 124 ' all offers two through holes, all is with insulation covering in the described through hole; Those positive and negative electrodes 123 ', 124 ' two insulation coverings are socketed in respectively on the positive and negative conducting rod 121 ', 122 ', and those positive and negative electrodes 123 ', 124 ' are evenly interval-staggered; Those positive mandrins 125 ' all conductive sleeve be connected on the positive conducting rod 121 ' and respectively conduction be abutted against those positive electrodes 123 ', those negative mandrins 126 ' all conductive sleeve be connected on the negative conducting rod 122 ' and respectively conduction be abutted against those negative potentials 124 '.Wherein: described positive and negative electrode interlocks and arranges at interval that evenly then interelectrode distance is little, and big, simple in structure, the saving material of electrode area then conducts electricity very well in the volume, and catalytic oxidation is effective, is particularly useful in the sewage degradation process.

Among the present embodiment, best, described positive mandrin 125 ' comprises two positive assistant director of a film or play's sheets, described two positive assistant director of a film or play's sheets two sides that all conductive sleeve is connected on the positive guide rod 121 ' and conduction abuts against corresponding positive electrode 123 ' respectively; Described negative mandrin 126 ' comprises two negative assistant director of a film or play's sheets, described two negative assistant director of a film or play's sheets two sides that all conductive sleeve is connected on the negative guide rod 122 ' and conduction abuts against corresponding negative potential 124 ' respectively.Wherein: connect positive and negative electrode by positive and negative assistant director of a film or play's sheet conduction, electrode does not have direct contact conduction and connects conducting rod, and then two conducting rods not only play the conduction ligation, but also play the positioning and fixing effect; Mandrin comprises two assistant director of a film or play's sheets, and two assistant director of a film or play's sheets conduct electricity two sides that abut against counter electrode respectively, then not only can conduct electricity connection electrode, and can also keeper electrode.

Among the present embodiment, best, all be provided with first insulating trip 127 ' that is socketed on the positive conducting rod between every adjacent positive assistant director of a film or play's sheet on the described positive conducting rod 121 ' and the negative potential; All be provided with second insulating trip 128 ' that is socketed on the negative conducting rod between every adjacent negative assistant director of a film or play's sheet on the described negative conducting rod 122 ' and the positive electrode.Wherein: all be provided with insulating trip between every adjacent assistant director of a film or play's sheet on the conducting rod and the electrode, then can avoid positive and negative electrode short circuit contact.

Among the present embodiment, best, described positive conducting rod 121 ' is a screw rod, and described positive assistant director of a film or play's sheet is nut type; Described negative conducting rod 122 ' is a screw rod, and described negative assistant director of a film or play's sheet is nut type.Among the present embodiment, best, described positive conducting rod 121 ' is a screw rod, and described first insulating trip 127 ' is nut type; Described negative conducting rod 122 ' is a screw rod, and described second insulating trip 128 ' is nut type.Wherein: conducting rod is a screw rod, and assistant director of a film or play's sheet, insulating trip are nut type, and is then easy to assembly, then can guarantee insulation, then can locate each device axial location.

Among the present embodiment, best, conduction is connected with an anodal plate 1211 ' of deriving on the described positive conducting rod 121 ', and conduction is connected with a negative pole and derives plate 1221 ' on the described negative conducting rod 122 '.Described anodal plate 1211 ' and the negative pole derivation plate 1221 ' of deriving conducts electricity two electrodes that are connected supervisory control desk respectively.

Among the present embodiment, best, also comprise at least one anti-short circuit insulation comb A, offer a plurality of evenly spaced insulation breach A1 on the described anti-short circuit insulation comb, the number of described insulation breach A1 equates with several 123 ', the 124 ' sums of positive and negative electrode, the interval pitch of described adjacent two insulation breach A1 and adjacent positive and negative electrode 123 ', 124 ' interval pitch are suitable, and described insulation breach A1 and positive electrode 123 ' or negative potential 124 ' are suitable.Wherein, anti-short circuit insulation comb can not play reinforcement effect, and can also prevent short circuit.

Wherein, second electrode device of described second electrocatalysis oxidation apparatus 200 can adopt the structure of first electrode device of first preferred embodiment, also can adopt the structure of first electrode device of second preferred embodiment.

The 3rd preferred embodiment

The present embodiment and the first preferred embodiment difference are:

Among the present embodiment, sewage disposal flows to and is: electric flocculation plant 300 ... first electrocatalysis oxidation apparatus 100 ... second electrocatalysis oxidation apparatus 200.Described electric flocculation plant 300 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, described first electrocatalysis oxidation apparatus 100 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, described second electrocatalysis oxidation apparatus 200 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, described electric flocculation plant 300 water-ins insert sewage, the water-in of described first electrocatalysis oxidation apparatus 100 is connected the water outlet of electric flocculation plant 300, and the water-in of described second electrocatalysis oxidation apparatus 200 is connected the water outlet of first electrocatalysis oxidation apparatus 100.The water outlet of described second electrocatalysis oxidation apparatus 200 is connected the water inlet of settler.

A kind of organic sewage environment-friendly treatment method, it comprises:

Step 10, electric flocculation step is separated out electrode ion and OH ion by the electrolysis process electrolysis, and flocculation agent is synthesized in described electrode ion and OH ionization, and described flocculation agent flocculates into wadding with sewage generation flocculation reaction with objectionable impurities in the sewage, and then precipitation;

Step 20, electrode catalytic oxidation step is separated out the OH ion by electrolysis process, and described OH ion is degraded into oxidation operation in the sewage can evaporable CO ₂And N ₂

Among the present embodiment, described step 10, it comprises:

Step 11, two electrode baskets 321 of described third electrode device 320 obtain electric energy, and the sewage liquid electrolytic in the flocculation container 310 is separated out the OH ion, and the electrode particle electrolysis in the electrode basket 321 is generated the electrode ion;

Step 12, described OH ion and electrode ionization synthetic flocculant;

Step 13, described flocculation agent flocculates into wadding with the generation flocculation reaction of sewage liquid with objectionable impurities in the sewage liquid, and then precipitation is in order to handling.

The 4th preferred embodiment

It and the first preferred embodiment difference are: a kind of organic sewage environment-friendly processing unit, please refer to Fig. 8, and it comprises one first electrocatalysis oxidation apparatus 100, one second electrocatalysis oxidation apparatus 200, a supply unit and a settler.Described first electrocatalysis oxidation apparatus 100 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top, and described second electrocatalysis oxidation apparatus 200 has the water outlet that a water-in and that is positioned at the bottom is positioned at the top.First electrocatalysis oxidation apparatus, 100 water-ins insert sewage, and the water-in of described second electrocatalysis oxidation apparatus 200 is connected the water outlet of first electrocatalysis oxidation apparatus 100.The water outlet of described second electrocatalysis oxidation apparatus 200 is connected the water inlet of settler.

The above, it only is the utility model preferred embodiment, so can not limit the scope that the utility model is implemented according to this, i.e. the equivalence of doing according to the utility model claim and description changes and modifies, and all should still belong in the scope that the utility model contains.

Claims

1. organic sewage environment-friendly processing unit, it is characterized in that: it comprises:

2. a kind of organic sewage environment-friendly processing unit according to claim 1 is characterized in that: described electrocatalysis oxidation apparatus is divided into first electrocatalysis oxidation apparatus and second electrocatalysis oxidation apparatus;

3. a kind of organic sewage environment-friendly processing unit according to claim 1 is characterized in that: described electrocatalysis oxidation apparatus is divided into first electrocatalysis oxidation apparatus and second electrocatalysis oxidation apparatus;

4. according to claim 2 or 3 described a kind of organic sewage environment-friendly processing units, it is characterized in that: it also comprises:

5. a kind of organic sewage environment-friendly processing unit according to claim 1, it is characterized in that: it also comprises:

6. a kind of organic sewage environment-friendly processing unit according to claim 1, it is characterized in that: it also comprises:

7. a kind of organic sewage environment-friendly processing unit according to claim 2, it is characterized in that: described settler comprises successively settling tank, precipitation vessel and settling pond side by side, all be provided with the scarfing cinder valve under described settling tank, precipitation vessel and the settling pond, described settling tank, precipitation vessel and settling pond all are provided with the spillway that a water-in and that is positioned at the bottom is located at the top; The water outlet of described second oxidation container is connected the water-in of settling tank, and the spillway of described settling tank is connected the water-in of precipitation vessel, and the spillway of described precipitation vessel is connected the water-in of settling pond.

8. a kind of organic sewage environment-friendly processing unit according to claim 3, it is characterized in that: described settler comprises successively settling tank, precipitation vessel and settling pond side by side, all be provided with the scarfing cinder valve under described settling tank, precipitation vessel and the settling pond, described settling tank, precipitation vessel and settling pond all are provided with the spillway that a water-in and that is positioned at the bottom is located at the top; The water outlet of described first oxidation container is connected the water-in of settling tank, and the spillway of described settling tank is connected the water-in of precipitation vessel, and the spillway of described precipitation vessel is connected the water-in of settling pond.

9. according to claim 7 or 8 described a kind of organic sewage environment-friendly processing units, it is characterized in that: it also comprises:

One adsorption unit, it comprises the contactor that flyash is housed in, it connects the scarfing cinder valve.