CN207142916U - A kind of anaerobic processing device of liquid debirs - Google Patents
A kind of anaerobic processing device of liquid debirs Download PDFInfo
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- CN207142916U CN207142916U CN201720813958.1U CN201720813958U CN207142916U CN 207142916 U CN207142916 U CN 207142916U CN 201720813958 U CN201720813958 U CN 201720813958U CN 207142916 U CN207142916 U CN 207142916U
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Abstract
The utility model discloses a kind of anaerobic processing device of liquid debirs, including retort, circulating pump and methane bag；The tank skin bottom of retort is provided with circulation discharging opening and circulation feeding mouth, circulation discharging opening is connected by first circulation pipe with the entrance of circulating pump, feeding mouth is circulated by second circulation pipe and the outlet of circulating pump, second circulation pipe is provided with steam inlet tube, and steam inlet tube is provided with magnetic valve；Liquid material inlet pipe, biogas outlet pipe and liquid material outlet pipe are additionally provided with the tank skin of retort, the inwall of liquid material inlet pipe is provided with supersonic generator, and biogas outlet pipe connects with methane bag；Agitating device is provided with retort, the bottom of retort is provided with temperature sensor.The utility model can pre-process to charging, by the agitating device in retort, liquid feedstock loop structure and to the temperature control in retort, improve degradation speed, make haptoreaction more abundant, realize the Effec-tive Function of anaerobic processing device.
Description
Technical field
It the utility model is related to field of waste water treatment, more particularly to a kind of anaerobic processing device of liquid debirs.
Background technology
With the rapid development of the national economy, substantial amounts of liquid debirs, environmental pollution are generated in industrial production
Cause and have a strong impact on, also constrain the development of relevant industries.Such as deal with improperly, the discharge of these waste liquids often leads to water body
Physics, chemistry and biological property change, and cause oxygen in water to decline, aquatile mortality, and produce rancid gas
Taste, high risks not only are caused to environment, are also brought about great losses to economy and society.
The biochemical treatment of waste water is the method that useless Organic substance in water is removed using the oxygenolysis of microorganism.According to institute
Requirement of the bacterium utilized to oxygen is different, biochemical treatment can be divided into Aerobic Process for Treatment and the major class of Anaerobic Treatment two.Anaerobic organism
Treatment technology has small investment, efficiency high, operating cost is low, need not supply oxygen, and power consumption is few, can produce the largely natural pond containing methane
Gas, available for the advantage such as low with family combustion gas, sludge yield that generates electricity, always all by environmental worker in water treatment field
Favor.
Existing anaerobic processing device passes through 120 years developments, undergoes significant innovation three times, however it remains influent quality will
Ask excessively strict, water distribution is uneven, degraded is insufficient, runs the problems such as mud phenomenon happens occasionally.So as to cause anaerobic processing device
Treatment effect it is unstable, influence the stability of whole Waste Water Treatment.
Therefore, how to ensure the Effec-tive Function of anaerobic processing device, be that current anaerobic processing device develops faced weight
Want problem.
Utility model content
For drawbacks described above, the purpose of this utility model is to provide a kind of anaerobic processing device of liquid debirs,
Charging is pre-processed, by the agitating device in retort, liquid feedstock loop structure and to the temperature control in retort
System, improves degradation speed, makes haptoreaction more abundant, realize the Effec-tive Function of anaerobic processing device.
The utility model to achieve the above object, is achieved through the following technical solutions：A kind of anaerobism of liquid debirs
Processing unit, it is characterised in that：Including retort, circulating pump and methane bag；The tank skin bottom of retort is provided with circulation discharging opening
With circulation feeding mouth, circulation discharging opening is connected by first circulation pipe with the entrance of circulating pump, and circulation feeding mouth follows by second
The outlet of endless tube and circulating pump, described second circulation pipe are provided with steam inlet tube, and steam inlet tube is provided with magnetic valve；Institute
Liquid material inlet pipe, biogas outlet pipe and liquid material outlet pipe are additionally provided with the tank skin for the retort stated, liquid material inlet pipe is provided with feed pump, liquid material
The inwall of inlet pipe is provided with supersonic generator, and biogas outlet pipe is located at the top of the tank skin of retort, and biogas outlet pipe connects with methane bag
Logical, liquid material outlet pipe is located between biogas outlet pipe and second circulation pipe；Agitating device, the bottom of retort are provided with described retort
Portion is provided with temperature sensor.
Further, described agitating device includes support and the agitator with motor, support are fixed on retort
Inwall on, motor is rack-mount, be sequentially provided with from top to bottom on the agitating shaft of agitator the first stirrer paddle and
Second stirrer paddle, the second stirrer paddle are located at agitating shaft bottom.
Further, be additionally provided with controller in described retort, controller respectively with temperature sensor, magnetic valve, charging
Pump, supersonic generator, motor connect with circulating pump.
Further, described liquid material outlet pipe is located at the top of the first stirrer paddle.
Further, it is equipped with control valve in described liquid material inlet pipe, biogas outlet pipe and liquid material outlet pipe.
Further, water seal is used at the top of described retort.
Further, described steam inlet tube is connected by three-way connection with second circulation pipe.
Prior art is contrasted, the utility model beneficial effect is：Liquid debirs provided by the utility model are detested
Oxygen processing unit, the tank skin bottom of retort are provided with circulation discharging opening and circulation feeding mouth, and circulation discharging opening passes through first circulation
Pipe connects with the entrance of circulating pump, and circulation feeding mouth is by second circulation pipe and the outlet of circulating pump, in the work of circulating pump
Under, interior circulation is formed on anaerobic processing device bottom, prevents that solid matter is in bottom precipitation in waste liquid, at the same can make charging with
Active microorganism quickly mixes in device；Second circulation pipe is provided with steam inlet tube, and steam inlet tube is provided with magnetic valve, passes through control
The conducting of steam inlet tube processed, realize the heating to liquid debirs in tank；The tank skin of retort is provided with liquid material inlet pipe, liquid
Material inlet pipe is provided with feed pump, and the inwall of liquid material inlet pipe is provided with supersonic generator, and liquid debirs are sent out by ultrasonic wave
Raw device enters retort after abolishing hard-degraded substance, reduces the solid impurity in liquid debirs, makes it easier to degrade；
Biogas outlet pipe and liquid material outlet pipe are additionally provided with the tank skin of retort, biogas outlet pipe is located at the top of the tank skin of retort, biogas outlet pipe
Connected with methane bag, can will decompose the collecting methane discharged, marsh gas power generation facility is used for after desulfurization and is generated electricity；Liquid material
Outlet pipe is located between biogas outlet pipe and second circulation pipe, can be imported the waste liquid that ullage is floated on after processing at squeezing processor
Reason；Agitating device is provided with retort, material is sufficiently mixed haptoreaction, degradation of organic substances with active microorganism in device
Matter；The bottom of retort is provided with temperature sensor, can monitor the liquid reactions temperature in tank in real time；Agitating device includes support
With the agitator with motor, support is fixed on the inwall of retort, and motor is rack-mount, agitator
The first stirrer paddle and the second stirrer paddle are sequentially provided with agitating shaft from top to bottom, the second stirrer paddle is located at agitating shaft bottom
End, is stirred, improves stirring efficiency simultaneously by two groups of stirrer paddles to different height in tank body；It is additionally provided with retort
Controller, controller connect with temperature sensor, magnetic valve, feed pump, supersonic generator, motor and circulating pump respectively
Connect, controller controls magnetic valve according to the data of temperature sensor, and then controls the importing of the steam in steam inlet tube, realizes
Temperature in tank is automatically controlled, ensures reaction temperature control in 35 ± 3 DEG C of optimal reaction temperature, moreover, it is achieved that controller
To the centralized Control of feed pump, supersonic generator, motor and circulating pump；Liquid material outlet pipe is located at the upper of the first stirrer paddle
Side, it ensure that derived waste liquid has been sufficiently agitated after processing and has floated on liquid level upper strata；Water seal, anti-leak-stopping are used at the top of retort
Gas, biogas leakage is avoided, pollutes air.
Brief description of the drawings
Accompanying drawing 1 is structural representation of the present utility model.
Accompanying drawing 2 is electrical diagram of the present utility model.
In figure, 1 is retort, and 11 be circulation discharging opening, and 12 be circulation feeding mouth, and 13 be temperature sensor, and 14 be control
Device, 2 be circulating pump, and 3 be agitating device, and 31 be support, and 32 be motor, and 33 be agitating shaft, and 34 be the first paddle, and 35 are
Second paddle, 4 be first circulation pipe, and 5 be second circulation pipe, and 6 liquid material inlet pipes, 61 be feed pump, and 62 be supersonic generator,
7 be steam inlet tube, and 71 be magnetic valve, and 8 be biogas outlet pipe, and 9 be liquid material outlet pipe, and 10 be methane bag.
Embodiment
Specific embodiment of the present utility model is explained below in conjunction with the accompanying drawings.
A kind of anaerobic processing device of liquid debirs as shown in Figure 1 and Figure 2, including retort 1, circulating pump 2 and natural pond
Airbag 10；The top of retort 1 uses water seal, and the tank skin bottom of retort 1 is provided with circulation discharging opening 11 and circulation feeding mouth 12, followed
Ring discharging opening 11 is connected by first circulation pipe 4 with the entrance of circulating pump 2, and circulation feeding mouth 12 is by second circulation pipe 5 with following
The outlet of ring pump 2, second circulation pipe 5 are provided with steam inlet tube 7, and steam inlet tube 7 passes through three-way connection and second circulation pipe 5
Connection, steam inlet tube 7 are provided with magnetic valve 71；Liquid material inlet pipe 6, biogas outlet pipe 8 and liquid material is additionally provided with the tank skin of retort 1 to go out
Pipe 9, liquid material inlet pipe 6 are provided with feed pump 61 and control valve, and the inwall of liquid material inlet pipe 6 is provided with supersonic generator 62, natural pond
Gas outlet pipe 8 is located at the top of the tank skin of retort 1, and biogas outlet pipe 8 is provided with control valve, and biogas outlet pipe 8 connects with methane bag 10,
Liquid material outlet pipe 9 is located between biogas outlet pipe 8 and second circulation pipe 5, and liquid material outlet pipe 9 is provided with control valve；Described retort 1
Interior to be provided with agitating device 3, agitating device 3 includes support 31 and the agitator with motor 32, and support 31 is fixed on reaction
On the inwall of tank 1, motor 32 is arranged on support 31, is sequentially provided with first from top to bottom on the agitating shaft 33 of agitator and is stirred
The stirrer paddle 35 of blade 34 and second is mixed, the second stirrer paddle 35 is located at the bottom of agitating shaft 33；Described liquid material outlet pipe 9 is located at
The top of one stirrer paddle 34, the bottom of retort 1 are provided with temperature sensor 13.
Be additionally provided with controller 14 in described retort 1, controller 14 respectively with temperature sensor 13, magnetic valve 71, enter
Material pump 61, supersonic generator 62, motor 32 and circulating pump 2 connect.
With reference to the drawings and specific embodiments, the utility model is described in further detail.It should be understood that these embodiments are only used for
Illustrate the utility model rather than limitation the scope of the utility model.In addition, it is to be understood that reading the utility model instruction
Content after, those skilled in the art can make various changes or modifications to the utility model, and these equivalent form of values equally fall
In scope defined herein.
Claims (7)
- A kind of 1. anaerobic processing device of liquid debirs, it is characterised in that：Including retort（1）, circulating pump（2）And biogas Bag（10）；Retort（1）Tank skin bottom be provided with circulation discharging opening（11）With circulation feeding mouth（12）, circulate discharging opening（11）It is logical Cross first circulation pipe（4）With circulating pump（2）Entrance connection, circulate feeding mouth（12）Pass through second circulation pipe（5）With circulating pump （2）Outlet, described second circulation pipe（5）It is provided with steam inlet tube（7）, steam inlet tube（7）It is provided with magnetic valve （71）；Described retort（1）Tank skin on be additionally provided with liquid material inlet pipe（6）, biogas outlet pipe（8）With liquid material outlet pipe（9）, liquid material enters Pipe（6）It is provided with feed pump（61）, liquid material inlet pipe（6）Inwall be provided with supersonic generator（62）, biogas outlet pipe（8）It is located at Retort（1）Tank skin at the top of, biogas outlet pipe（8）With methane bag（10）Connection, liquid material outlet pipe（9）It is located at biogas outlet pipe（8）With Second circulation pipe（5）Between；Described retort（1）It is interior to be provided with agitating device（3）, retort（1）Bottom provided with temperature pass Sensor（13）.
- 2. the anaerobic processing device of liquid debirs according to claim 1, it is characterised in that：Described agitating device （3）Including support（31）With with motor（32）Agitator, support（31）It is fixed on retort（1）Inwall on, drive Dynamic motor（32）Installed in support（31）On, the agitating shaft of agitator（33）On be sequentially provided with the first stirrer paddle from top to bottom （34）With the second stirrer paddle（35）, the second stirrer paddle（35）It is located at agitating shaft（33）Bottom.
- 3. the anaerobic processing device of liquid debirs according to claim 2, it is characterised in that：Described retort （1）On be additionally provided with controller（14）, controller（14）Respectively with temperature sensor（13）, magnetic valve（71）, feed pump（61）, it is super Sonic generator（62）, motor（32）And circulating pump（2）Connection.
- 4. the anaerobic processing device of liquid debirs according to claim 2, it is characterised in that：Described liquid material outlet pipe （9）It is located at the first stirrer paddle（34）Top.
- 5. the anaerobic processing device of liquid debirs according to claim 1, it is characterised in that：Described liquid material inlet pipe （6）, biogas outlet pipe（8）With liquid material outlet pipe（9）On be equipped with control valve.
- 6. the anaerobic processing device of liquid debirs according to claim 1, it is characterised in that：DescribedRetort（1）Top uses water seal.
- 7. the anaerobic processing device of liquid debirs according to claim 1, it is characterised in that：Described steam inlet tube （7）Pass through three-way connection and second circulation pipe（5）Connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720813958.1U CN207142916U (en) | 2017-07-06 | 2017-07-06 | A kind of anaerobic processing device of liquid debirs |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720813958.1U CN207142916U (en) | 2017-07-06 | 2017-07-06 | A kind of anaerobic processing device of liquid debirs |
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| CN207142916U true CN207142916U (en) | 2018-03-27 |
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| CN201720813958.1U Active CN207142916U (en) | 2017-07-06 | 2017-07-06 | A kind of anaerobic processing device of liquid debirs |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847640A (en) * | 2020-07-15 | 2020-10-30 | 安徽省环境科学研究院 | Improved IC reaction equipment capable of being adjusted in use and use method thereof |
-
2017
- 2017-07-06 CN CN201720813958.1U patent/CN207142916U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847640A (en) * | 2020-07-15 | 2020-10-30 | 安徽省环境科学研究院 | Improved IC reaction equipment capable of being adjusted in use and use method thereof |
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