CN205710077U - Anaerobic Waste Treatment System - Google Patents
Anaerobic Waste Treatment System Download PDFInfo
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- CN205710077U CN205710077U CN201620541201.7U CN201620541201U CN205710077U CN 205710077 U CN205710077 U CN 205710077U CN 201620541201 U CN201620541201 U CN 201620541201U CN 205710077 U CN205710077 U CN 205710077U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
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Abstract
This utility model provides a kind of Anaerobic Waste Treatment System, and including flowing back into water pot, flowing back into water pot connection has the inlet channel for being passed through pending waste water；Anaerobic reactor, flows back into water pot and is communicated to anaerobic reactor by frequency conversion inlet water lifting pumps；And going out water pot, anaerobic reactor is communicated to out in water pot via water outlet pipeline, and goes out water pot and be communicated to flow back into water pot.Native system is by integrated to anaerobic reactor tank body, water outlet tank body, tank body of intaking, and Highgrade integration and automatization simplify the operation maintenance work of Anaerobic Waste Treatment System.
Description
Technical field
This utility model relates in general to field of waste water treatment, more specifically, particularly relate to a kind of organic containing high concentration
Pollutant and the biochemical treatment of wastewater of noxious substance.
Background technology
The anaerobic treatment of waste water is a kind of efficient wastewater processing technology, is to process waste water to utilize with energy recovery
A kind of biochemical technology combined.Anaerobic bio-treated is to utilize the vital metabolic of anaerobe, is being not required to the premise of oxygen supply
Lower organic pollution in waste water being converted into the materials such as water, methane, carbon dioxide and new cyton, wherein methane is that one can
The energy recycled.
As long as the development experience of anaerobic technology century more than one.Within 1896, there is First for processing life dirt in Britain
The anaerobic digester of water, produced biogas is used for street lighting.Mid-term the 1950's occurs in that Anaerobic Contact reactor,
It is additionally arranged sludge refluxing apparatus so that it is treatment effeciency and load significantly improve.Since 20 century 70s, agriculture university of Holland
The up-flow anaerobic sludge blanket (being called for short UASB) of Lettinga et al. invention, is the quantum jump in anaerobic technology development history, becomes
For the anaerobic treatment method being most widely used at present, it is for second filial generation anaerobic treatment process.The new and effective anaerobism of the third generation is anti-
Answer device with anaerobic expanded granular sludge bed reactor (EGSB), inner circulation reactor (IC) as representative, be in recent years at UASB base
The anaerobic reactor improved on plinth, the operating load compared to UASB all improves a lot.Novel new and effective reactor phase
Following improvement is had: (1) uses granule sludge, has had vast improvement, make reactor in microbial morphology compared with traditional reactor
Unit volume Biomass is higher, and mud is prone to sedimentation, and effluent quality is preferable；(2) higher ratio of height to diameter and upflow velocity, reactor
Endoparticle mud presents swelling state so that between muddy water, mass transfer effect is more preferable；(3) relatively larger ratio of height to diameter so that reactor takes up an area
Area is less.
And in the prior art, the improvement making a general survey of all kinds of reactor is all that reactor itself is made various optimization, seldom
Someone makes optimization in the technological process of anaerobic treatment reactor.
Utility model content
For problem present in correlation technique, the purpose of this utility model be to provide a kind of by anaerobic reactor, go out
Water pot and flow back into the Anaerobic Waste Treatment System that water pot is integrated.
For achieving the above object, this utility model provides a kind of Anaerobic Waste Treatment System.
Anaerobic Waste Treatment System of the present utility model, including: flowing back into water pot, flowing back into water pot connection has water inlet pipe
Road；Anaerobic reactor, flows back into water pot and is communicated to anaerobic reactor by frequency conversion inlet water lifting pumps；And going out water pot, anaerobism is anti-
Answer device to be communicated to out in water pot via water outlet pipeline, and go out water pot and be communicated to flow back into water pot.
According to Anaerobic Waste Treatment System of the present utility model, the import and export of frequency conversion inlet water lifting pumps are respectively connecting to backflow
The bottom of water inlet tank and the water inlet of anaerobic reactor；And
The top going out water pot connects water outlet pipeline, goes out water pot and is connected to flow back into the side of water pot by backflow overflow line
Wall, and the bottom going out water pot is connected to flow back into the bottom of water pot via sludge reflux pipeline.
According to Anaerobic Waste Treatment System of the present utility model, water outlet pipeline is connected to the water conservancy diversion being arranged on out in water pot
Cylinder, wherein, arranges tube settling mechanism, and the overflow of the overflow line that refluxes between outer wall and the inwall going out water pot of guide shell
Port is exposed by the top of tube settling mechanism.
According to Anaerobic Waste Treatment System of the present utility model, the top going out water pot is additionally provided with out water pot liquidometer, and
And the bottom going out water pot is additionally provided with out water pot mud level meter, wherein, the gas going out water pot mud level meter with being positioned on sludge reflux pipeline
The dynamic chain setting of switch valve.
According to Anaerobic Waste Treatment System of the present utility model, the sidewall connection going out water pot has water outlet pipeline, water outlet pipeline
Position higher than tube settling mechanism top and less than reflux overflow line overflow port, water outlet pipeline is provided with water outlet
Effusion meter and pneumatic control valve, wherein, pneumatic control valve with flow back into water pot fluid level for monitoring flow back into water pot
The chain setting of liquidometer.
According to Anaerobic Waste Treatment System of the present utility model, flow back into water pot and be internally provided with agitator, and reflux
Water inlet tank is additionally provided with overflow line.
According to Anaerobic Waste Treatment System of the present utility model, inlet channel is provided with inlet channel effusion meter and water inlet pipe
Road pneumatic control valve, wherein, inlet channel pneumatic control valve and the backflow water inlet of fluid pH value in monitoring flows back into water pot
The chain setting of tank pH meter.
According to Anaerobic Waste Treatment System of the present utility model, being additionally provided with firing equipment in flowing back into water pot, heating sets
For connecting to have on steam pipe line, and steam pipe line, steam pipe line pneumatic control valve is set, wherein, steam pipe line pneumatic control valve
With flow back into fluid temperature (F.T.) in water pot by monitoring flow back into chain setting based on water tank temperature.
According to Anaerobic Waste Treatment System of the present utility model, flow back into water pot and be connected to frequency conversion via pump water inlet pipeline and enter
Water elevator pump, and frequency conversion inlet water lifting pumps is connected to anaerobic reactor via water pump outlet pipe line, and wherein, water pump outlet pipe line connects
To being positioned at the cloth wetting system of anaerobic reactor, wherein, water pump outlet pipe line connects there is water pump outlet pipe linear flow rate meter.
According to Anaerobic Waste Treatment System of the present utility model, anaerobic reactor arranges three phase separator, and anaerobism
Reactor is additionally provided with based on the reactor pH meter by monitoring wherein pH value, temperature and liquid level, temperature of reactor and reactor liquid
Position meter, wherein, reactor pH meter and temperature of reactor meter and the chain setting of inlet channel pneumatic control valve, reactor liquidometer with
The chain setting of frequency conversion inlet water lifting pumps.
According to Anaerobic Waste Treatment System of the present utility model, anaerobic reactor top is additionally provided with biogas pipeline, wherein,
Biogas pipeline has in biogas line pressure table and biogas effusion meter, and biogas pipeline and is also associated with spark arrester.
According to Anaerobic Waste Treatment System of the present utility model, the bottom sidewall of anaerobic reactor is additionally provided with emptying/row
Mud pipeline.
Having the beneficial effects that of Anaerobic Waste Treatment System of the present utility model:
Anaerobic Waste Treatment System of the present utility model, including flowing back into water pot, flowing back into water pot connection has inlet channel；
Anaerobic reactor, flows back into water pot and is communicated to anaerobic reactor by frequency conversion inlet water lifting pumps；And go out water pot, anaerobic reactor
It is communicated to out in water pot via water outlet pipeline, and goes out water pot and be communicated to flow back into water pot.This programme by anaerobic reactor tank body,
Going out water pot and to flow back into water pot integrated, Highgrade integration and automatization simplify the operation maintenance work of anaerobic reactor
Make.
Accompanying drawing explanation
Fig. 1 is the structural representation of an embodiment of Anaerobic Waste Treatment System of the present utility model.
Detailed description of the invention
In conjunction with accompanying drawing, Waste Water Treatment of the present utility model is described.Specifically, Fig. 1 is of the present utility model
The structural representation of the embodiment of Anaerobic Waste Treatment System.As it is shown in figure 1, the Waste Water Treatment of the present embodiment, including returning
Flowing to water pot 4, anaerobic reactor 20 and go out water pot 29, wherein, flowing back into water pot 4 connection has inlet channel 1；Flow back into water pot
4 are communicated to anaerobic reactor 20 by frequency conversion inlet water lifting pumps 14；Anaerobic reactor 20 is communicated to water outlet via water outlet pipeline 30
In tank 29, and go out water pot 29 and be communicated to flow back into water pot 4.
The Waste Water Treatment of the present embodiment, including flowing back into water pot, flowing back into water pot connection has inlet channel；Anaerobism is anti-
Answer device, flow back into water pot and be communicated to anaerobic reactor by frequency conversion inlet water lifting pumps；And going out water pot, anaerobic reactor is via going out
Water pipeline is communicated to out in water pot, and goes out water pot and be communicated to flow back into water pot.This programme by anaerobic reactor tank body, go out water pot
Integrated with flowing back into water pot, Highgrade integration and automatization simplify the operation maintenance work of anaerobic reactor.
On the basis of the embodiment of the above-mentioned Waste Water Treatment of the present utility model shown in Fig. 1, this practicality is new
Type can also specifically include herein below.
In certain embodiments, the import and export of frequency conversion inlet water lifting pumps 14 be respectively connecting to flow back into water pot 4 bottom and
The water inlet of anaerobic reactor 20, wherein, frequency conversion inlet water lifting pumps 14 promotes water pump for anaerobic reactor water inlet, and goes out water pot
The top of 29 connects water outlet pipeline 30, goes out water pot 29 and is connected to flow back into the sidewall of water pot 4 by backflow overflow line 31, and
The bottom going out water pot 29 is connected to flow back into the bottom of water pot 4 via sludge reflux pipeline 34.
In certain embodiments, water outlet pipeline 30 is connected to the guide shell 33 being arranged on out in water pot 29, and guide shell 33 sets
Putting in the centre going out water pot 29, guide shell 33 upper end connects with water outlet pipeline, and lower end passes to out the bottom of water pot 29, is used for
Water outlet is guided to out bottom water pot 29.Wherein, between outer wall and the inwall going out water pot 29 of guide shell 33, tube settling is set
Mechanism 32, the sludge retention in the waste water derived by guide shell 33 is to going out the bottom of water pot 29, and the overflow line that refluxes
The overflow port of 31 is exposed by the top of tube settling mechanism 32, and backflow overflow line 31 lower end is communicated to flow back into water pot 4,
Flow back into water pot 4 for being flowed backward to by recycling effluent.
In certain embodiments, the top going out water pot 29 is additionally provided with out water pot liquidometer 28, and goes out the end of water pot 29
Portion is additionally provided with out water pot mud level meter 9, wherein, the pneumatic on-off valve going out water pot mud level meter 9 with being positioned on sludge reflux pipeline 34
35 chain settings.
In certain embodiments, the sidewall connection going out water pot 29 has water outlet pipeline 36, and wherein the position of water outlet pipeline 36 is high
In the top of tube settling mechanism 32 and less than backflow overflow line 31 overflow port.In other words, water outlet pipeline 36 entrance
End is positioned at the top of tube settling mechanism 32, is used for deriving waste water, is provided with water flow meter 38 and pneumatic in water outlet pipeline 36
Regulation valve 37, wherein, pneumatic control valve 37 with flow back into water pot 4 fluid level for monitoring flow back into water pot liquidometer 8
Chain setting.
In certain embodiments, flowing back into water pot 4 and be internally provided with agitator 7, agitator 7 will be for flowing back in water pot
Waste water and the waste water mixing of loop backflow, and flow back into water pot 4 and be additionally provided with overflow line 10.
In certain embodiments, inlet channel 1 is used for importing waste water to flowing back into water pot, and inlet channel 1 be provided with into
Waterpipe effusion meter 2 and inlet channel pneumatic control valve 3, for regulating entrance and the inlet of waste water.Wherein, inlet channel gas
In moving regulation valve 3 and flowing back into water pot 4 for monitoring, fluid pH value flows back into the chain setting of water pot pH meter 6.
In certain embodiments, being additionally provided with firing equipment in flowing back into water pot 4, firing equipment connects steam pipe line
12, vapor line 12 arranges the pneumatic regulation of steam pipe line for importing on the steam needed for adding apparatus, and steam pipe line 12
Valve 11, wherein, steam pipe line pneumatic control valve 11 with flow back into water pot 4 for monitoring in fluid temperature (F.T.) flow back into water tank temperature
Count 5 chain settings.Firing equipment is arranged on the bottom flowing back into water pot, for being heated by the waste water flowed back in water pot.
In certain embodiments, flow back into water pot 4 and be connected to frequency conversion inlet water lifting pumps 14 via pump water inlet pipeline 13, and
Frequency conversion inlet water lifting pumps 14 is connected to anaerobic reactor 20 via water pump outlet pipe line 16, and wherein, water pump outlet pipe line 16 is connected to position
Cloth wetting system 17 in anaerobic reactor 20, wherein, water pump outlet pipe line 16 connects and has water pump outlet pipe linear flow rate meter 15.
In certain embodiments, anaerobic reactor 20 arranges three phase separator 18, and anaerobic reactor 20 also sets up
Have based on the reactor pH meter 21 by monitoring wherein pH value, temperature and liquid level, temperature of reactor 22 and reactor liquidometer 23, its
In, reactor pH meter 21 and temperature of reactor meter 22 and the chain setting of inlet channel pneumatic control valve 3, reactor liquidometer 23 with
The chain setting of frequency conversion inlet water lifting pumps 14.
In certain embodiments, anaerobic reactor 20 top is additionally provided with biogas pipeline 24, and wherein, biogas pipeline 24 has
Biogas line pressure table 25 and biogas effusion meter 26, and biogas pipeline 24 are also associated with spark arrester 27.In some embodiments
In, the bottom sidewall of anaerobic reactor 20 is additionally provided with emptying/mud delivery pipeline 19.
The operation principle of Waste Water Treatment of the present utility model is described below: high concentrated organic wastewater passes through inlet channel
1 entrance flows back in water pot 4, and on inlet channel 1, inlet channel effusion meter 2 and inlet channel pneumatic control valve 3 record and control
System amount of inlet water, go out simultaneously recycling effluent in water pot 29 also in flowing back into water pot 4 and under the effect of agitator 7 with
System has been intake and has uniformly been mixed and dilute.Flow back into the firing equipment in water pot 4 determine whether to set up according to inflow temperature and
The waste water flowed back in water pot 4 is heated, to promote inflow temperature and the thermal loss of supplementary recycling effluent, maintains the reflux for
In water inlet tank 4, water temperature is between 35 DEG C-38 DEG C.
The water flowed back in water pot 4 is squeezed in anaerobic reactor 20 by frequency conversion inlet water lifting pumps 14, completes the anaerobism of waste water
Biochemical treatment.The regulation of anaerobic reactor 20 amount of inlet water is completed to realize reflux ratio, upper up-flow by changing variable frequency pump frequency
The regulation of speed.
The guide shell 33 that the water outlet of anaerobic reactor 20 enters into out in water pot 29 is interior by anaerobic reactor 20 water outlet water conservancy diversion
To going out bottom water pot 29, sludge retention in water outlet is settled down to by the tube settling facility 32 then flowed through in water outlet in water outlet tank 29
Go out in water pot 29 base sludge district.Recycling effluent after tube settling facility 32 precipitates, overflows through going out water pot 29 upper return
Flow tube line 31 enters in flowing back into water pot 4 and completes mixed diluting with system water, and system water outlet is then by water outlet pipeline 36 and pipe
Outside pneumatic control valve 37 on line and water flow meter 38 are with the flow discharge system of the water yield in entrance system.Go out in water pot 29
Water pot mud level meter 9 is set out, go out water pot mud level meter 9 chain go out pneumatic on-off valve on water pot 29 base sludge reflux pipeline 34
35, open pneumatic on-off valve 35 when going out water pot 29 inner bottom part sludge blanket and reaching and set high mud position, go out the mud in water pot 29 certainly
Dynamic entrance flows back in water pot 4；Pneumatic on-off valve 35 is closed when the sludge blanket flowed back in water pot 4 reaches to set low mud position.
Enter the mud flowing back in water pot 4 and enter in anaerobic reactor 20 with processing after water mixes by frequency conversion inlet water lifting pumps 14,
It is automatically performed out the backflow of sewage sludge.
Waste Water Treatment of the present utility model provides the benefit that: (1) passes through vast scale effluent recycling, is remarkably improved
System inlet COD concentration, is not required to introduce dilution water, be remarkably improved the COD load impact of reactor, enter for high-concentration waste water
Coolant-temperature gage impact, noxious substance impact tolerance；(2) anaerobic reactor 20 upflow velocity, reflux ratio can easily be accommodated, at one
In anaerobic reactor 20, anaerobic grain sludge can reach as desired expand or fluidized state thus formed EGSB reactor or on
Streaming anaerobic fluidized bed reactor；(3) go out water pot 29 to arrange tube settling facility 32 and solve anaerobic reactor 20 and easily run mud
Problem so that effluent quality is preferable；(4) intake pump of anaerobic reactor 20 and backflow water pump be integrated minimizing number of devices and
Construction investment；(5) by anaerobic reactor 20, go out water pot 29, to flow back into water pot 4 integrated, Highgrade integration and automatization
Simplify anaerobic reactor 20 operation maintenance work.
This utility model is made further elucidated above with embodiment below in conjunction with the accompanying drawings.
Seeing Fig. 1, the complete system for anaerobic treatment of a kind of high concentrated organic wastewater of this utility model is anti-by anaerobism with method
Answer device 20, water inlet system, outlet system, return-flow system integrated.High concentrated organic wastewater is entered back by inlet channel 1
Flowing in water pot 4 body, on inlet channel 1, inlet channel effusion meter 2 and inlet channel pneumatic control valve 3 record and show and control
System amount of inlet water, go out simultaneously the recycling effluent in water pot 29 also through backflow overflow line 31 enter flow back in water pot 4 and
Intake with system under the effect of agitator 7 and uniformly mixed and dilute.Flow back into the heating facility in water pot 4 body according to water inlet
Temperature determines whether to set up to heat the waste water flowed back in water pot 4 water, with promote inflow temperature and supplement reflux out
The thermal loss of water, flows back into water tank temperature meter 5 chain steam pipe line pneumatic control valve 11, by steam pipe line pneumatic control valve
The valve opening of 11, in regulation and control flow back into water pot 4, water temperature is maintained between 35 DEG C-38 DEG C, when temperature is less than 35 DEG C, steam pipe line
Pneumatic control valve 11 aperture tunes up, and when temperature is higher than 38 DEG C, steam pipe line pneumatic control valve 11 aperture is turned down, when temperature is higher than
When 40 DEG C, steam pipe line pneumatic control valve 11 cuts out.
Flow back into water pot PH meter 6 monitoring constantly and flow back into the pH of water in water pot 4, carry out when pH is more than 8.5 or less than 6.5
Reporting to the police, when pH is more than 9.0 or is less than 6.0, chain inlet channel pneumatic control valve 3 makes it cut out, and stops water inlet.
Flowing back into water pot liquidometer 8 to monitor constantly and flow back into the liquid level of water in water pot 4, when liquid level, to be in low liquid level (or high
Liquid level) the most chain pneumatic control valve of alarm 37 turns its aperture down (or tuning up), pneumatic when liquid level is recovered to normal liquid level
Regulation valve 37 stops regulation aperture, chain frequency conversion inlet water lifting pumps 14 termination of pumping when liquid level is in low liquid level.When liquid level is in
During high level, in flowing back into water pot 4, water is outside the automatic outflow system of overflow line 10, and simultaneity factor sends warning.
The water flowed back in water pot 4 is filled with detests through pump water inlet pipeline 13 and water pump outlet pipe line 16 by frequency conversion inlet water lifting pumps 14
In oxygen reactor 20, completing the anaerobic biochemical treatment of waste water, anaerobic reactor 20 inflow passes through water pump outlet pipe linear flow rate meter 15
Record and show.The regulation of anaerobic reactor 20 amount of inlet water is completed with reality by changing frequency conversion inlet water lifting pumps 14 frequency
Existing reflux ratio, the regulation of upflow velocity.
Such as the label in Fig. 1,17 is water distribution system, and 18 is three phase separator, and 19 is blow-down pipe and mud delivery pipeline, and 20 are
Anaerobic reactor, 24 is biogas pipeline, and 25 is biogas line pressure table, and to show biogas line pressure, 26 is biogas effusion meter,
With record and display biogas flow, 27 is spark arrester.PH in anaerobic reactor 20 monitored constantly by reactor pH meter 21, when pH is more than
8.5 or less than 6.5 time report to the police, when pH more than 9.0 or less than 6.0 time chain pneumatic inlet channel pneumatic control valve 2 make it
Close, stop water inlet.Temperature in anaerobic reactor 20 monitored constantly by temperature of reactor meter 22, when temperature is less than 35 DEG C, and pneumatic tune
Joint valve 37 aperture tunes up, and when temperature is higher than 38 DEG C, pneumatic control valve 37 aperture is turned down, when temperature is higher than 40 DEG C, and pneumatic tune
Joint valve 37 cuts out.Liquid level in anaerobic reactor 20 monitored constantly by reactor liquidometer 23.High liquid level warning, the chain frequency conversion of high level
Inlet water lifting pumps 14 termination of pumping, low liquid level warning.
By anaerobic reactor in anaerobic reactor 20 water outlet guide shell 33 in water outlet pipeline 30 enters into out water pot 29
20 water outlets are guided to out bottom water pot 29, then flow through the tube settling facility 32 in water outlet tank 29 in water outlet by mud in water outlet
Retain and be settled down to out in water pot 29 base sludge district.Recycling effluent after inclined tube 32 precipitates, through going out water pot 29 upper return
Overflow line 31 enters in flowing back into water pot 4 and completes mixed diluting with system water, system water outlet then by water outlet pipeline 36 and
Outside pneumatic control valve 37 on pipeline and water flow meter 38 are to similarly enter the flow discharge system of the system water yield.Water outlet
Water pot mud level meter 9 is set out in tank 29.Go out water pot mud level meter 9 chain go out pneumatic on water pot 29 base sludge reflux pipeline 34 open
Close valve 35, open pneumatic on-off valve 35 when going out water pot 29 inner bottom part sludge blanket and reaching and set high mud position, go out the dirt in water pot 29
Mud is automatically into flowing back in water pot 4；Pneumatic on-off valve is closed when the sludge blanket flowed back in water pot 4 reaches to set low mud position
35.Enter the mud flowing back in water pot 4 and enter in anaerobic reactor 20 with processing after water mixes by frequency conversion intake pump 14, from
Move out of the backflow of sewage sludge.Go out water pot mud level meter 9 and detect the liquid level in water pot 29, high level alarm, high liquid constantly
Chain frequency conversion inlet water lifting pumps 14 termination of pumping during position, low liquid level warning.
The foregoing is only preferred embodiment of the present utility model, be not limited to this utility model, for this
For the technical staff in field, this utility model can have various modifications and variations.All in spirit of the present utility model and principle
Within, any modification, equivalent substitution and improvement etc. made, within should be included in protection domain of the present utility model.
Claims (12)
1. an Anaerobic Waste Treatment System, it is characterised in that including:
Flow back into water pot (4), described in flow back into water pot (4) connect have the inlet channel (1) for being passed through pending waste water；
Anaerobic reactor (20), described in flow back into water pot (4) and be communicated to described anaerobic reaction by frequency conversion inlet water lifting pumps (14)
Device (20)；And
Go out water pot (29), described anaerobic reactor (20) via water outlet pipeline (30) be communicated to described in go out in water pot (29), and
Described go out water pot (29) be communicated to described in flow back into water pot (4).
Anaerobic Waste Treatment System the most according to claim 1, it is characterised in that
The import and export of described frequency conversion inlet water lifting pumps (14) flow back into the bottom of water pot (4) and described anaerobism described in being respectively connecting to
The water inlet of reactor (20)；And
Described go out water pot (29) top connect described water outlet pipeline (30), described in go out water pot (29) by backflow overflow line
(31) be connected to described in flow back into the sidewall of water pot (4), and described in go out the bottom of water pot (29) via sludge reflux pipeline
(34) be connected to described in flow back into the bottom of water pot (4).
Anaerobic Waste Treatment System the most according to claim 2, it is characterised in that
Described water outlet pipeline (30) be connected to be arranged on described in go out in water pot (29) guide shell (33),
Wherein, the outer wall of described guide shell (33) and described go out water pot (29) inwall between tube settling mechanism (32) is set,
And the overflow port of described backflow overflow line (31) is exposed by the top of described tube settling mechanism (32).
Anaerobic Waste Treatment System the most according to claim 3, it is characterised in that
Described go out water pot (29) top be additionally provided with out water pot liquidometer (28), and described in go out the bottom of water pot (29) and also set
It is equipped with out water pot mud level meter (9),
Wherein, the pneumatic on-off valve (35) going out water pot mud level meter (9) described in and be positioned on described sludge reflux pipeline (34) is chain
Arrange.
Anaerobic Waste Treatment System the most according to claim 3, it is characterised in that
Described go out water pot (29) sidewall connect have water outlet pipeline (36), the position of described water outlet pipeline (36) be higher than described inclined tube
Precipitate the top of mechanism (32) and be less than the overflow port of described backflow overflow line (31), described water outlet pipeline (36) is arranged
There are water flow meter (38) and pneumatic control valve (37),
Wherein, described pneumatic control valve (37) be used for monitoring described in flow back into water pot (4) fluid level flow back into water pot
Liquidometer (8) chain setting.
Anaerobic Waste Treatment System the most according to claim 1, it is characterised in that
The described water pot (4) that flows back into is internally provided with agitator (7), and described in flow back into water pot (4) and be additionally provided with overflow pipe
Line (10).
Anaerobic Waste Treatment System the most according to claim 1, it is characterised in that
Described inlet channel (1) is provided with inlet channel effusion meter (2) and inlet channel pneumatic control valve (3),
Wherein, described inlet channel pneumatic control valve (3) flows back into the backflow of water pot (4) interior fluid pH value described in being used for monitoring
Water inlet tank pH meter (6) chain setting.
Anaerobic Waste Treatment System the most according to claim 1, it is characterised in that
Described flow back into water pot (4) in be additionally provided with firing equipment, described firing equipment connects steam pipe line (12), and institute
State and steam pipe line pneumatic control valve (11) be set on steam pipe line (12),
Wherein, described steam pipe line pneumatic control valve (11) flows back into returning of water pot (4) interior fluid temperature (F.T.) described in being used for monitoring
Flow to water tank temperature meter (5) chain setting.
Anaerobic Waste Treatment System the most according to claim 1, it is characterised in that
The described water pot (4) that flows back into is connected to described frequency conversion inlet water lifting pumps (14) via pump water inlet pipeline (13), and described
Frequency conversion inlet water lifting pumps (14) is connected to described anaerobic reactor (20) via water pump outlet pipe line (16),
Wherein, described water pump outlet pipe line (16) is connected to be positioned at the cloth wetting system (17) of described anaerobic reactor (20),
Wherein, the upper connection of described water pump outlet pipe line (16) has water pump outlet pipe linear flow rate meter (15).
Anaerobic Waste Treatment System the most according to claim 7, it is characterised in that
Described anaerobic reactor (20) arranges three phase separator (18), and described anaerobic reactor (20) be additionally provided with for
Monitor the reactor pH meter (21) of wherein pH value, temperature and liquid level, temperature of reactor meter (22) and reactor liquidometer (23),
Wherein, described reactor pH meter (21) and described temperature of reactor meter (22) and described inlet channel pneumatic control valve (3)
Chain setting, described reactor liquidometer (23) and the chain setting of described frequency conversion inlet water lifting pumps (14).
11. Anaerobic Waste Treatment System according to claim 10, it is characterised in that
Described anaerobic reactor (20) top is additionally provided with biogas pipeline (24),
Wherein, described biogas pipeline (24) has biogas line pressure table (25) and biogas effusion meter (26), and described biogas
Pipeline (24) is also associated with spark arrester (27).
12. Anaerobic Waste Treatment System according to claim 11, it is characterised in that
The bottom sidewall of described anaerobic reactor (20) is additionally provided with emptying/mud delivery pipeline (19).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620541201.7U CN205710077U (en) | 2016-06-06 | 2016-06-06 | Anaerobic Waste Treatment System |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620541201.7U CN205710077U (en) | 2016-06-06 | 2016-06-06 | Anaerobic Waste Treatment System |
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| Publication Number | Publication Date |
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| CN205710077U true CN205710077U (en) | 2016-11-23 |
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| CN201620541201.7U Active CN205710077U (en) | 2016-06-06 | 2016-06-06 | Anaerobic Waste Treatment System |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105936545A (en) * | 2016-06-06 | 2016-09-14 | 中国石油集团东北炼化工程有限公司吉林设计院 | Wastewater anaerobic treatment system |
-
2016
- 2016-06-06 CN CN201620541201.7U patent/CN205710077U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105936545A (en) * | 2016-06-06 | 2016-09-14 | 中国石油集团东北炼化工程有限公司吉林设计院 | Wastewater anaerobic treatment system |
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