CN105036325A - Multi-phase reinforcement and guide type circular and anaerobic granulation reaction processing device - Google Patents
Multi-phase reinforcement and guide type circular and anaerobic granulation reaction processing device Download PDFInfo
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Abstract
The invention relates to a multi-phase reinforcement and guide type circular and anaerobic granulation reaction processing device applied to high concentrated organic wastewater. The processing device is characterized by comprising a water inlet assembly, a water outlet assembly, a processing device body, a biogas processing assembly and an internal circulation assembly, wherein the biogas processing assembly is arranged on the processing device body, and the internal circulation assembly is arranged in the processing device body; the water inlet assembly is arranged at the lower part of the processing device body, and the water outlet assembly is arranged at the upper part of the processing device body. The processing device has the beneficial effects that the integral structural design is skillful, and the operation is convenient; the rapid granulation of anaerobic sludge in the treatment process of high concentrated organic wastewater is realized by virtue of multiple granulated fillers, internal and external circulation, efficient water distribution and cyclic heating of wastewater, so that the anaerobic debugging time is shortened, meanwhile, the volumetric load and removal rate of an anaerobic reaction device for treating high concentrated organic wastewater are substantially improved, and the construction cost of the anaerobic reaction device is lowered.
Description
Technical field
The present invention relates to a kind of wastewater treatment equipment, be specifically related to a kind of heterogeneous strengthening for high concentrated organic wastewater and divide and lead circulation anaerobic granular sludge reaction unit, belong to technical field of sewage.
Background technology
Along with industrial boom, kind and the quantity of waste water rapidly increase, also increasingly extensive and serious to the pollution of water body, threaten the health and safety of the mankind.High concentrated organic wastewater is the one of trade effluent, complicated component, and some is also toxic, more difficult also more important than municipal sewage treatment; The hazardness of the high concentrated organic wastewater that industry produces is mainly reflected in three aspects, one is aerobism harm: due to biological degradation, high concentrated organic wastewater can make receiving water body anoxic even anaerobism, and most aquatic organism is by death, thus generation stench, worsen water quality and environment; Two is organoleptic pollutions: high concentrated organic wastewater not only makes water body lose use value, more has a strong impact on the orthobiosis of the nearby water bodies people; Three is causing toxicity harm: containing a large amount of toxic organic compound in ultra-high concentration organic wastewater, constantly can accumulate, store, finally enter human body, be detrimental to health in the physical environment such as water body, soil.
Technology of High Concentration OrganicWastewater Treatment is divided into roughly 3 classes: materializing strategy technology, chemical treatment method and biologic treating technique, specific as follows:
(1) materializing strategy technology: a kind of pretreated means of physico-chemical process Chang Zuowei are applied to treatment of Organic Wastewater, pretreated object is the useful component by reclaiming in waste water, or some difficult for biological degradation things are processed, thus reach organics removal, improve biochemical, reduce biochemical treatment load, improve processing efficiency.General conventional physico-chemical process has extraction process, absorption method, method of enrichment etc.Extraction process is simple, is suitable for the organism processing recovery value, but can only be used for nonpolar organic matter, and the organism be extracted and the waste water after extracting need process further, and organic solvent also may cause secondary pollution.Extraction is the physical transfer process of a pollutent, and the degraded of really.The sorbent material that absorption method is commonly used in organic waste water has gac and macroporous resin, although gac has higher adsorptivity, owing to regenerating difficulty, costly and at home less use.Method of enrichment is simple to operate, technical maturity, and can realize the partially recycled of useful matter, is suitable for processing treating high-concentration saline organic wastewater, and the shortcoming of this method is that energy consumption is high.
(2) chemical treatment method
:chemical treatment method is that the pollutant component in waste water is converted into innoxious substance by applied chemistry principle and chemical action, makes the method that waste water is purified.Chemical oxidization method is divided into two large classes, and a class utilizes strong oxidizer (as hydrogen peroxide, potassium permanganate, hypochlorite, ozone etc.) that the oxidation operation in waste water is become carbonic acid gas and water at normal temperatures and pressures; Another kind of is organism in Decomposition Wastewater at high temperature under high pressure, and comprise supercritical water oxidation and wet-air oxidation technique, oxygenant used is generally oxygen or hydrogen peroxide, and the general catalyzer that adopts reduces reaction conditions, accelerates speed of reaction; Chemical oxidization method speed of response is fast, control is simple, but cost is higher, is usually difficult to by the organism oxidation step of difficult degradation to inorganic substance, and less to the research of the control of intermediate product at present.This technology also usually uses as the pretreatment process of biochemical treatment.Its main method has burning method, Fenton oxidation method, Ozonation, electrochemical oxidation process etc.
(3) biologic treating technique: biological treatment is the main technique of purification of waste water, mainly for the treatment of the organic waste water of the industries such as agricultural chemicals, printing and dyeing, pharmacy.Biological treatment is the biotechnology utilizing the metabolism of microorganism to decompose, transform toxic and harmful substance in water body and other various component that exceeds standard, the place of Degradation is mainly containing microbic activity mud, microbial film and corresponding reactor thereof, and be born different kind organism treatment technology thus.Microbial method is economy, safety not only, and the pollutent threshold value of process is low, residual less, non-secondary pollution, has good application prospect.According to the difference of reaction conditions, microorganism treatment can be divided into Aerobic biological process and the large class of anaerobic biological treatment two.The change of Aerobic biological process to waste water quality, the water yield has stronger adaptability, better to the organic matter removal effect in waste water, but Aerobic biological process needs aeration oxygen supply, and energy consumption is larger, in being applicable to, the process of low-concentration organic waste water, for high concentration organic sewage, there is intractability.Anaerobic biological treatment is a kind of sewage disposal technology with very large application prospect, especially in high concentration wastewater treatment field.Under many circumstances, anaerobic technique is the first-selected technique of the wastewater treatment under process high loading, subsidence volumn limited circumstances.Relative to Aerobic biological process method, anaerobic technique does not need separately to add oxygen source, and working cost is low, and surplus sludge volume is few, and organic loading is high.Its main drawback is that speed of response is slower, reaction times is longer, process structures volume is large, the cycle that starts is long, the scarce capacity for the treatment of S S, be difficult to form granule sludge etc. during process high-concentration waste water, but these methods of the prior art are difficult to process to high concentrated organic wastewater, and the treatment time is long, be difficult to form granule sludge, therefore, a kind of new technical scheme of exigence solves the technical problem existed in prior art.
Summary of the invention
In order to solve above-mentioned Problems existing, the invention discloses a kind of heterogeneous strengthening for high concentrated organic wastewater to divide and lead circulation anaerobic granulating reaction treating device, this device overall construction design is ingenious, easy to operate, utilize multiple granulating filler, inner-outer circulation, efficient water distribution and waste water circulation heating realize the quick particle of anaerobic sludge in high concentrated organic wastewater treating processes to shorten anaerobism initial failure period, increase substantially volumetric loading and the clearance of anaerobic reaction device process high concentrated organic wastewater simultaneously, reduce the construction cost of anaerobic reaction device.
To achieve these goals; technical scheme of the present invention is as follows; a kind of heterogeneous strengthening for high concentrated organic wastewater divides leads circulation anaerobic granulating reaction treating device; it is characterized in that; described treatment unit comprises water inlet component, outlet component; treatment unit body; be arranged on the biogas treatment assembly on treatment unit body and be arranged on the internal recycle assembly for the treatment of unit body interior; described water inlet component is arranged on the bottom for the treatment of unit body, and described outlet component is arranged on the top for the treatment of unit body.Be provided with granulating filler in described treatment unit body, granulating filler is made up of gac, zeolite, Wingdale and slag, and admission space is 5% of reaction treating device useful volume.The particle diameter of granulating filler is 0.5 ~ 1.0mm; admission space is than being gac: zeolite: Wingdale: slag is 6:2:1:1; arrange like this and can make full use of on the one hand the treatment effect that gac and the huge specific surface area of zeolite improve reaction unit, also can reduce processing cost to a certain extent on the other hand.Granulating filler, as the nucleus of condensation of granule sludge, forms granule sludge for making in anaerobic device fast.Gac and zeolite, owing to having larger specific surface area, as the nucleus of condensation of granule sludge, can make anaerobic sludge quick particle; Wingdale and slag, as a part for granule sludge composition, can increase the incompressible intensity of granule sludge, make granule sludge be not easy fragmentation.This technical scheme adopts the technical scheme of inner-outer circulation backflow and high-efficiency rotating water distribution, and realize the abundant contact of muddy water, biochemical treatment is short for start time, sludge blockage phenomenon in alleviator simultaneously, shorten the treatment time, improve processing efficiency, reduce enterprise cost.
As a modification of the present invention, described water inlet component comprises water inlet pipe, intake pump, valve, well heater and high-efficiency rotating water distributor, the adjacent one end of described water inlet pipe is provided with intake pump, valve and well heater, the water inlet pipe the other end stretches into the bottom for the treatment of unit body, and the other end of water inlet pipe is provided with high-efficiency rotating water distributor.Water inlet pipe is connected with high-efficiency rotating water distributor with valve by intake pump, and high-efficiency rotating water distributor is used for the abundant mixing of muddy water, shortens biochemical treatment start time, alleviates the latch up phenomenon of mud in device simultaneously.
As a modification of the present invention, described outlet component comprises rising pipe and overflow weir, and described rising pipe is connected by valve with overflow weir.
As a modification of the present invention, described internal recycle assembly comprises Marsh gas collecting hood, up-flow guide, Jiang Liu district, baffling cap, sludge bucket, described baffling cap is positioned at the top of up-flow guide, and described Marsh gas collecting hood is positioned at the bottom of up-flow guide, and described sludge bucket is positioned at the below of Marsh gas collecting hood.Wherein Marsh gas collecting hood is used for the biogas that bottom collection device, anaerobic sludge is formed, the biogas produced drives bottom muddy water under the effect of up-flow guide, complete the internal recycle in up-flow district and Jiang Liu district, up-flow guide top arranges the recoil of baffling cap for feed liquid, realize the automatic pulverizing of scum silica frost and foam, the problems such as foam that solution layering, scum silica frost are crusted and feed liquid rises, strengthen water conservancy diversion simultaneously and improve muddy water internal recycle effect; Circulating pipe is connected with water inlet pipe with valve by water circulating pump, can accelerate granular sludge process by controlled circulation water upflow velocity, and circulating pipe is arranged on and can reduces its impact on triphase separator water outlet clarifying effect in the middle part of device.
As a modification of the present invention, described reaction treating device also comprises triphase separator, and described triphase separator is arranged on the top for the treatment of unit body, and described triphase separator is used for the three phase separation of biogas, waste water and mud.
As a modification of the present invention, described triphase separator is made up of upper and lower three layers of deflecting plate, deflecting plate is herring-bone, spacing between neighbouring deflecting plate is 15cm, deflecting plate and deflecting plate angle are 55 °, be staggered, arrange like this and gas-liquid can be made more easily to be blocked backflow by solid during deflecting plate, thus improve the effect of biogas, waste water and mud three phase separation.
As a modification of the present invention, described biogas treatment assembly comprises collecting methane pipe, methane purifying device and firedamp drainage pipe, described methane purifying device is arranged between collecting methane pipe and firedamp drainage pipe, described collecting methane pipe one end connects triphase separator, and the other end connects methane purifying device.
As a modification of the present invention, the below of described treatment unit body is provided with shore pipe, for the discharge of excess sludge in device; The side of described treatment unit body is also provided with circulating pipe, and described circulating pipe is provided with water circulating pump, one end connection handling device body of described circulating pipe, and the other end connects water inlet pipe.Circulating pipe is connected with water inlet pipe with valve by water circulating pump, can accelerate granular sludge process by controlled circulation water upflow velocity, and circulating pipe is arranged on and can reduces its impact on triphase separator water outlet clarifying effect in the middle part of device.
Relative to prior art, advantage of the present invention is as follows, 1) whole Technical Design is ingenious, compact construction, cost is lower, 2) this technical scheme adopts inner-outer circulation backflow and high-efficiency rotating water distribution technology, realizes the abundant contact of muddy water, biochemical treatment is short for start time, simultaneously sludge blockage phenomenon in alleviator; 3) the granulating filler in this technical scheme adopts four kinds of granulating filler compositions as the nucleus of condensation of anaerobic sludge, the quick particle of anaerobic sludge in high concentrated organic wastewater can be realized, increase the incompressible intensity of anaerobic grain sludge simultaneously, anaerobic device starts to occur granule sludge when running about 1.5 months, and anaerobic sludge settling property significantly improves; 4) this technical scheme up-flow guide top arranges the recoil of baffling cap for feed liquid, can realize the automatic pulverizing of scum silica frost and foam, solves layering, scum silica frost crust to rise the problems such as foam with feed liquid, strengthens water conservancy diversion simultaneously and improves muddy water internal recycle effect; 5) this device is good to the removal effect of COD and SS, to the clearance > 92% of high concentrated organic wastewater COD, to the clearance > 25% of SS; And the clearance of existing anaerobic technology to COD is only about 80%, substantially removal effect is not had to SS; 6) this technical scheme is adaptable to water quality, water yield change, and volumetric loading can reach 10 ~ 20kgCOD/m
3.d, be conventional anaerobic device volumetric loading 3 ~ 5kgCOD/m
3.d 2 ~ 5 times, the construction cost of device can greatly be reduced; 7) this technical scheme anaerobic reaction is abundant, and biogas output is large, and biogas is recoverable after purifying treatment, and recycling economy is strong, greatly reduces enterprise cost; 8) this plant automation degree is high, effective, instant effect, simple to operate, compact construction, and floor space is little, applied widely, and plant running is stablized, and cost is lower, long service life, maintenance are more convenient.
Accompanying drawing explanation
Fig. 1 is one-piece construction schematic diagram of the present invention;
In figure: 1 water inlet pipe, 2 intake pumps, 3 valves, 4 well heaters; 5 water circulating pumps, 6 circulating pipes, 7 baffling caps, 8 rising pipes; 9 overflow weirs, 10 collecting methane pipes, 11 methane purifying devices, 12 firedamp drainage pipes; 13 triphase separators, 14 up-flow guides, 15 Jiang Liu districts; 16 Marsh gas collecting hoods, 17 sludge buckets, 18 granulating fillers; 19 high-efficiency rotating water distributors, 20 shore pipes, 21 treatment unit bodies.
Embodiment
In order to deepen, to understanding of the present invention and understanding, below in conjunction with the drawings and specific embodiments, to illustrate the present invention further.
embodiment 1:
See Fig. 1, a kind of heterogeneous strengthening for high concentrated organic wastewater divides leads circulation anaerobic granulating reaction treating device, described treatment unit comprises water inlet component, outlet component, treatment unit body 21, be arranged on the biogas treatment assembly on treatment unit body 21 and be arranged on the internal recycle assembly for the treatment of unit body interior, described water inlet component is arranged on the bottom for the treatment of unit body, and described outlet component is arranged on the top for the treatment of unit body; Described water inlet component comprises water inlet pipe 1, intake pump 2, valve 3, well heater 4 and high-efficiency rotating water distributor 19, the adjacent one end of described water inlet pipe 1 is provided with intake pump 2, valve 3 and well heater 4, the water inlet pipe the other end stretches into the bottom for the treatment of unit body, and the other end of water inlet pipe is provided with high-efficiency rotating water distributor 19.Water inlet pipe 1 is connected with high-efficiency rotating water distributor 19 with valve 3 by intake pump 2, high-efficiency rotating water distributor 19 is for the abundant mixing of muddy water, shorten biochemical treatment start time, alleviate the latch up phenomenon of mud in device simultaneously, described outlet component comprises rising pipe 8 and overflow weir 9, and described rising pipe 8 is connected by valve with overflow weir 9.Described treatment unit body is always provided with granulating filler 18; described granulating filler is made up of gac, zeolite, Wingdale and slag; admission space is 5% of reaction treating device useful volume; the particle diameter of described granulating filler is 0.5 ~ 1.0mm; admission space is than being gac: zeolite: Wingdale: slag is 6:2:1:1; arrange like this and can make full use of on the one hand the treatment effect that gac and the huge specific surface area of zeolite improve reaction unit, also can reduce processing cost to a certain extent on the other hand.Granulating filler, as the nucleus of condensation of granule sludge, forms granule sludge for making in anaerobic device fast.Gac and zeolite, owing to having larger specific surface area, as the nucleus of condensation of granule sludge, can make anaerobic sludge quick particle; Wingdale and slag, as a part for granule sludge composition, can increase the incompressible intensity of granule sludge, make granule sludge be not easy fragmentation.This technical scheme adopts the technical scheme of inner-outer circulation backflow and high-efficiency rotating water distribution, and realize the abundant contact of muddy water, biochemical treatment is short for start time, sludge blockage phenomenon in alleviator simultaneously, shorten the treatment time, improve processing efficiency, reduce enterprise cost.
embodiment 2:
See Fig. 1, as a modification of the present invention, described internal recycle assembly comprises Marsh gas collecting hood 16, up-flow guide 14, Jiang Liu district 15, baffling cap 7, sludge bucket 17, described baffling cap 7 is positioned at the top of up-flow guide 14, described Marsh gas collecting hood 16 is positioned at the bottom of up-flow guide 14, and described sludge bucket 17 is positioned at the below of Marsh gas collecting hood 16.Wherein Marsh gas collecting hood 16 is for the biogas of anaerobic sludge formation bottom collection device, the biogas produced drives bottom muddy water under the effect of up-flow guide, complete the internal recycle in up-flow district and Jiang Liu district, up-flow guide top arranges the recoil of baffling cap for feed liquid, realize the automatic pulverizing of scum silica frost and foam, the problems such as foam that solution layering, scum silica frost are crusted and feed liquid rises, strengthen water conservancy diversion simultaneously and improve muddy water internal recycle effect; Circulating pipe is connected with water inlet pipe with valve by water circulating pump, can accelerate granular sludge process by controlled circulation water upflow velocity, and portion arranges circulating pipe to reduce its impact on triphase separator water outlet clarifying effect in a device.All the other structures are identical with embodiment 1 with advantage.
embodiment 3:
See Fig. 1, as a modification of the present invention, described reaction treating device also comprises triphase separator 13, and described triphase separator 13 is arranged on the top for the treatment of unit body 21, and described triphase separator 13 is for the three phase separation of biogas, waste water and mud.All the other structures are identical with embodiment 1 with advantage.
embodiment 4:
See Fig. 1, as a modification of the present invention, described triphase separator 13 is made up of upper and lower three layers of deflecting plate, deflecting plate is herring-bone, spacing between neighbouring deflecting plate is 15cm, and deflecting plate and deflecting plate angle are 55 °, are staggered, arrange like this and gas-liquid can be made more easily to be blocked backflow by solid during deflecting plate, thus improve the effect of biogas, waste water and mud three phase separation.All the other structures are identical with embodiment 1 with advantage.
embodiment 5:
See Fig. 1, as a modification of the present invention, described biogas treatment assembly comprises collecting methane pipe 10, methane purifying device 11 and firedamp drainage pipe 12, described methane purifying device 11 is arranged between collecting methane pipe 10 and firedamp drainage pipe 12, described collecting methane pipe 10 one end connects triphase separator 13, and the other end connects methane purifying device 11.All the other structures are identical with embodiment 1 with advantage.
embodiment 6:
See Fig. 1, as a modification of the present invention, the below of described treatment unit body is provided with shore pipe 20, for the discharge of excess sludge in device; The side of described treatment unit body 21 is also provided with circulating pipe 6, and described circulating pipe 6 is provided with water circulating pump 5, one end connection handling device body 21 of described circulating pipe 6, and the other end connects water inlet pipe 1.Circulating pipe is connected with water inlet pipe with valve by water circulating pump, can accelerate granular sludge process by controlled circulation water upflow velocity, and portion arranges circulating pipe to reduce its impact on triphase separator water outlet clarifying effect in a device.All the other structures are identical with embodiment 1 with advantage.
principle of work:as shown in Figure 1; for the reaction treating device of high concentrated organic wastewater; high concentrated organic wastewater mixes through water inlet pipe 1 and circulating pipe 5 bottom being entered anaerobic grain reaction unit after heater via 4 heating by high-efficiency rotating water distributor 19, and recirculated water controls upflow velocity by water circulating pump 5.Improve water treatment effect for making to generate granule sludge in anaerobic reaction device fast, control device circulation upflow velocity is 0.2 ~ 0.3m/h, and controlling sludge seeding amount is 30000 ~ 40000mg/L, and control wastewater temperature is 35 DEG C simultaneously; Anaerobic device initial operating stage volumetric loading is ascending to be increased gradually, as the clearance > 80% of anaerobic device to COD, volumetric loading increases in the ratio of 30%, and organic acid (VAF) content <8mmol/L in control device.Gac, zeolite, Wingdale and slag four kinds of granulating fillers 18 are loaded, as the nucleus of condensation of anaerobic grain sludge, for shortening the formation time of granule sludge bottom anaerobic reaction device.The anaerobic sludge of high concentrated organic wastewater and bottom of device constantly reacts, a large amount of biogas can be produced, biogas after Marsh gas collecting hood 16 is collected drives the muddy water bottom anaerobic device to rise, under the effect of up-flow guide 14, baffling cap 7, Jiang Liu district 15 and sludge bucket 17, complete the internal recycle of wastewater treatment, thus greatly improve the removal effect of Pollutants in Wastewater.The biogas produced, after triphase separator 13 is separated, is collected by collecting methane pipe 10, and biogas is discharge or utilization after methane purifying device 11 processes.Mud after triphase separator 13 is separated, enters the bottom of anaerobic reaction device, carries out the waste water circulation process of next round through Jiang Liu district 15.Waste water after anaerobic reaction device process discharges or enters the wastewater treatment of next stage through overflow weir 9 and rising pipe 8, and the excess sludge that anaerobic reaction device produces is discharged by shore pipe 20.
application example 1:
Table 1 is the process example of Hebei biodiesel wastewater:
The process example of table 1 Hebei biodiesel wastewater
Heterogeneous strengthening divides leads circulation anaerobic granulating reaction unit for the treatment of Hebei biodiesel wastewater, and can reach 94.7% and 27.1% respectively to the clearance of COD and SS, now the volumetric loading of anaerobic device is 12.9kgCOD/m
3.d, be conventional anaerobic device volumetric loading 3 ~ 5kgCOD/m
3.d 2 ~ 5 times, anaerobic device starts to occur granule sludge when operation about 1.5 months.
application example 2:
Table 2 is process examples of Jiangsu Wastewater in Biologic Pharmacy, and contained by the waste water before and after this device process, pollutent contrast is as follows:
The process example of table 2 Jiangsu Wastewater in Biologic Pharmacy
Heterogeneous strengthening divides leads circulation anaerobic granulating reaction unit for the treatment of Jiangsu Wastewater in Biologic Pharmacy, and can reach 93.2% and 25.4% respectively to the clearance of COD and SS, now the volumetric loading of anaerobic device is 11.3kgCOD/m
3.d, be conventional anaerobic device volumetric loading 3 ~ 5kgCOD/m
3.d 2 ~ 5 times, anaerobic device starts to occur granule sludge when operation about 1.5 months.
application example 3:
Table 3 is process examples of Jiangsu Wastewater From The Beverage Industry, and contained by the waste water before and after this device process, pollutent contrast is as follows:
The process example of table 3 Jiangsu Wastewater From The Beverage Industry
Heterogeneous strengthening divides leads circulation anaerobic granulating reaction unit for the treatment of Jiangsu Wastewater From The Beverage Industry, and can reach 92.1% and 25.2% respectively to the clearance of COD and SS, now the volumetric loading of anaerobic device is 10.2kgCOD/m
3.d, be conventional anaerobic device volumetric loading 3 ~ 5kgCOD/m
3.d 2 ~ 5 times, anaerobic device starts to occur granule sludge when running about January.
Can find out, the content of the above-mentioned Wastewater Pollutant after this device process reduces greatly, and this apparatus design is reasonable, and can not produce secondary pollution in treating processes, cost is lower, is convenient to apply on a large scale.
At least one in technical characteristic described in embodiment 2,3,4,5,6 and embodiment 1 can also combine by the present invention, form new embodiment.
It should be noted that, above-described embodiment is only preferred embodiment of the present invention, be not used for limit protection scope of the present invention, the equivalent replacement that the basis of technique scheme is made or substitute, all belong to protection scope of the present invention.
Claims (10)
1. a heterogeneous strengthening divides and leads circulation anaerobic granulating reaction treating device; it is characterized in that; described treatment unit comprises water inlet component, outlet component; treatment unit body; be arranged on the biogas treatment assembly on treatment unit body and be arranged on the internal recycle assembly for the treatment of unit body interior; described water inlet component is arranged on the bottom for the treatment of unit body, and described outlet component is arranged on the top for the treatment of unit body.
2. heterogeneous strengthening according to claim 1 divides and leads circulation anaerobic granulating reaction treating device; it is characterized in that; described water inlet component comprises water inlet pipe, intake pump, valve, well heater and high-efficiency rotating water distributor; the adjacent one end of described water inlet pipe is provided with intake pump, valve and well heater; the water inlet pipe the other end stretches into the bottom for the treatment of unit body, and the other end of water inlet pipe is provided with high-efficiency rotating water distributor.
3. heterogeneous strengthening according to claim 2 divides and leads circulation anaerobic granulating reaction treating device, and it is characterized in that, described outlet component comprises rising pipe and overflow weir, and described rising pipe is connected by valve with overflow weir.
4. the heterogeneous strengthening according to Claims 2 or 3 divides leads circulation anaerobic granulating reaction treating device; it is characterized in that; described internal recycle assembly comprises Marsh gas collecting hood, up-flow guide, Jiang Liu district, baffling cap, sludge bucket; described baffling cap is positioned at the top of up-flow guide; described Marsh gas collecting hood is positioned at the bottom of up-flow guide, and described sludge bucket is positioned at the below of Marsh gas collecting hood.
5. heterogeneous strengthening according to claim 4 divides and leads circulation anaerobic granulating reaction treating device, and it is characterized in that, described reaction treating device also comprises triphase separator, and described triphase separator is arranged on the top for the treatment of unit body.
6. heterogeneous strengthening according to claim 5 divides and leads circulation anaerobic granulating reaction treating device; it is characterized in that; described triphase separator is made up of upper and lower three layers of deflecting plate; deflecting plate is herring-bone; spacing between neighbouring deflecting plate is 15cm; deflecting plate and deflecting plate angle are 55 °, are staggered.
7. heterogeneous strengthening according to claim 6 divides and leads circulation anaerobic granulating reaction treating device; it is characterized in that; described biogas treatment assembly comprises collecting methane pipe, methane purifying device and firedamp drainage pipe; described methane purifying device is arranged between collecting methane pipe and firedamp drainage pipe; described collecting methane pipe one end connects triphase separator, and the other end connects methane purifying device.
8. heterogeneous strengthening according to claim 7 divides and leads circulation anaerobic granulating reaction treating device; it is characterized in that; granulating filler is provided with in described sludge bucket; described granulating filler is made up of gac, zeolite, Wingdale and slag, and admission space is 5% of reaction treating device useful volume.
9. heterogeneous strengthening according to claim 8 divides and leads circulation anaerobic granulating reaction treating device, and it is characterized in that, the particle diameter of described granulating filler is 0.5 ~ 1.0mm, and admission space is than being gac: zeolite: Wingdale: slag is 6:2:1:1.
10. the heterogeneous strengthening according to claim 7 or 8 or 9 divides leads circulation anaerobic granulating reaction treating device; it is characterized in that; the below of described treatment unit body is provided with shore pipe; the side of described treatment unit body is also provided with circulating pipe; described circulating pipe is provided with water circulating pump; one end connection handling device body of described circulating pipe, the other end connects water inlet pipe.
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| CN107670638A (en) * | 2017-09-30 | 2018-02-09 | 武汉金钢新材料有限公司 | Steel mill's waste residue composition for filtration treatment sewage and preparation method thereof |
| CN108996680A (en) * | 2018-09-30 | 2018-12-14 | 中国环境科学研究院 | Modular assembly type anaerobic fermentation tower apparatus and its method for handling organic wastewater |
| CN110845008A (en) * | 2019-10-09 | 2020-02-28 | 浙江省天正设计工程有限公司 | Bioreactor for treating high-salt organic wastewater based on composite salt-tolerant strains |
| CN113631520A (en) * | 2018-12-31 | 2021-11-09 | 中国石油化工股份有限公司 | Solid precipitation device and solid precipitation method |
| CN115583726A (en) * | 2022-11-03 | 2023-01-10 | 中国石油化工股份有限公司 | Anaerobic reactor for sewage treatment and use method thereof |
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| CN108996680A (en) * | 2018-09-30 | 2018-12-14 | 中国环境科学研究院 | Modular assembly type anaerobic fermentation tower apparatus and its method for handling organic wastewater |
| CN113631520A (en) * | 2018-12-31 | 2021-11-09 | 中国石油化工股份有限公司 | Solid precipitation device and solid precipitation method |
| CN110845008A (en) * | 2019-10-09 | 2020-02-28 | 浙江省天正设计工程有限公司 | Bioreactor for treating high-salt organic wastewater based on composite salt-tolerant strains |
| CN115583726A (en) * | 2022-11-03 | 2023-01-10 | 中国石油化工股份有限公司 | Anaerobic reactor for sewage treatment and use method thereof |
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