CN201581072U - Sludge discharge device - Google Patents
Sludge discharge device Download PDFInfo
- Publication number
- CN201581072U CN201581072U CN2009202199813U CN200920219981U CN201581072U CN 201581072 U CN201581072 U CN 201581072U CN 2009202199813 U CN2009202199813 U CN 2009202199813U CN 200920219981 U CN200920219981 U CN 200920219981U CN 201581072 U CN201581072 U CN 201581072U
- Authority
- CN
- China
- Prior art keywords
- water body
- output channel
- flushing pump
- sparger
- soil discharging
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
The utility model discloses a sludge discharge device, which belongs to the field of sludge discharge devices of biogas engineering, and solves the defects that an existing device can not thoroughly and smoothly discharge sludge, and does not have ideal sludge discharge effect and the like. The the utility model aims to supply a spraying type sludge discharge device which is beneficial to discharge sludge for the biogas engineering, and increases the production rate of anaerobic reaction devices and the volume gas production rate of raw materials. The sludge discharge device comprises a control system, a washing pump, a water body main input pipeline, a water body distributor, a water body partial output pipeline and a gate valve, wherein the control system is connected with the washing pump, the gate valve and a check valve through electric signals, and the water body distributor is arranged on a position of the middle portion of the lower portion in a reactor. The washing pump is connected with the upper portion of the reactor through the water body main input pipeline, the washing pump is connected with the water body distributor through the water body main output pipeline, and the gate valve is arranged on a pipeline of a passageway of the washing pump.
Description
Technical field
The utility model relates to soil discharging facility, belongs to biogas engineering soil discharging facility field.
Background technology
In the anaerobic reactor of big-and-middle-sized biogas engineering, the common natural sedimentation of fermented feed liquid and be divided into 4 layers is respectively scum layer, supernatant layer, active coating and sediment layer from top to bottom.Fermentation container at existing used for biogas project does not generally all have sludge drainage system, all is in tank base a shore pipe only to be installed substantially, and the self gravitation of expecting by fermentation comes spoil disposal.Advantage is laborsaving, uncomplicated, but shortcoming is long-time curing easily, and spoil disposal is not smooth, and the effect of spoil disposal is undesirable, causes the waste residue waste material to take a big chunk useful volume of fermentor tank, thereby influences factor of created gase.
The equipment that some sludge treatment are also arranged in the prior art, as 00,211,058 1 kinds of Vertical Restrain Sludge Digestion Devices of Chinese patent, by pond body, shore pipe, carriage, vertical tube bank, supernatant liquor vent pipe, upflow tube, biogas output tube, upper cover body, advance the mud pipe and form, be characterized in that carriage is positioned at the pond body, and connect with the bottom pool wall, vertical tube bank is positioned at the pond body, and its lower surface and carriage join.This device changes reaction conditions owing in the body of pond vertical tube bank is set, and the turbulent shear that mud produced when biogas passed through tube bank is strong, accelerates digester anaerobic reaction speed and efficient; 00,235,023 1 kinds of folded plate type vertical passageway sludge digestions of Chinese patent device, by pond body, shore pipe, carriage, flap vertical passageway, supernatant liquor vent pipe, upflow tube, biogas output tube, upper cover body, advance the mud pipe and form, be characterized in that carriage is positioned at the pond body, and connect with the bottom pool wall, the flap vertical passageway is positioned at the pond body, and its lower surface and carriage join.This device is owing to be provided with the flap vertical passageway in the body of pond, change reacting dynamics condition, the turbulent shear that mud produced when biogas passed through the flap vertical passageway is strong, accelerate digester anaerobic reaction speed and efficient, its processing efficiency is far longer than conventional sludge digestion tank, shortens the time of mud at digester.Defectives such as but these equipment also exist spoil disposal not thorough, and spoil disposal is not smooth, and the effect of spoil disposal is undesirable.
The utility model content
Exist spoil disposal not thorough in order to overcome existing equipment, spoil disposal is not smooth, defectives such as the effect of spoil disposal is undesirable, a purpose of the present utility model is: provide a kind of spraying type soil discharging facility that helps the biogas engineering spoil disposal, with the productivity that improves this anaerobic reaction equipment and the volume factor of created gase of raw material.
The technical scheme that its technical problem that solves the utility model adopts is as follows: the soil discharging facility that is connected with reactor comprises that Controlling System, flushing pump, water body primary input pipeline, water body sparger, water body divide output channel, gate valve; Described Controlling System is connected by electrical signal with flushing pump, gate valve, reverse checkvalve; Described water body sparger is positioned at reactor, the bottom position intermediate; Flushing pump is connected with reactor top by water body primary input pipeline, and flushing pump is connected with the water body sparger by water body master output channel; Described gate valve is positioned on the water body primary input pipeline of ingress of flushing pump, and on the water body master output channel in exit.Described water body divides output channel to be connected with the water body sparger.
Also comprise stopping valve, reverse checkvalve, described stopping valve 7 is positioned at the part of water body master output channel near flushing pump; Reverse checkvalve is positioned at the exit that water body primary input pipeline, water body master output channel and water body divide output channel.
The inlet of described flushing pump communicates with the supernatant layer place on reactor top by water body primary input pipeline, and described flushing pump outlet is connected with the water body sparger by water body master output channel;
Described Controlling System comprises power distribution cabinet, control panel, and power distribution cabinet is connected by electrical signal with control panel; Described electrical signal transmits by the electric wire transmission or by wireless device, preferred wire equipment.
The inlet of described flushing pump, outlet all communicate with reactor through pipeline; On the pipeline of the ingress of flushing pump gate valve is housed, on the pipeline in exit gate valve is housed, the gate valve role is for controlling flushing pump neatly.
Supernatant layer place in the inlet of described flushing pump and the reactor communicates; Described flushing pump outlet communicates with the water body output channel, and the water body output channel communicates with the water body sparger; Described water body sparger divides output channel to communicate with water body, and control valve all is housed, to control the switching at the place that respectively communicates.
Divide the outlet of output channel to be equipped with elbow at described each water body, by elbow straight current are become the current with angle, current just can make the current of flushing form the whirlpool shape after having certain angle, could wash thoroughly, bend angle α is 10-80 °, preferred 15-45 °, more preferably 25-35 °, most preferably 30 °.
The bending direction unanimity of described elbow, all along clockwise direction or counterclockwise crooked.
Described each hydraulic pipe, promptly main body hydraulic pipe and split hydraulic pipe refer to 2 and 4) the exit reverse checkvalve all is housed, avoid liquid under the effect of pressure, to produce backflow phenomenon and pollute and stop up water pipe.
It is two or more that water body divides output channel, is the center with the water body sparger, evenly distributed, and water body divides output channel to communicate with the inside of water body sparger.
Water body divides preferred 6 of output channel, is the center with the water body sparger, and it is 60 ° that evenly distributed each water body divides the angle between the output channel.
Compared with prior art, the beneficial effects of the utility model are:
1. the utility model has adopted spray equipment, comprises flushing pump, vacuum breaker, and water body spargers etc. strengthen rinse capability, make sludge removal more thorough.
2. divide the outlet of output channel to be equipped with elbow at described each water body, by elbow straight current are become the current with angle, current make the current of flushing form the whirlpool shape after having certain angle, increase rinse capability, can wash reactor thoroughly, especially bend angle is in the time of 25-35 °, the whirlpool rinse capability highly significant that current form.
3. by scientific structure of the present utility model, can improve factor of created gase, the application of flushing pump makes impact force of water flow strong in the utility model, make current form whirlpool by elbow, make impulse force reach each angle of reactor, farthest avoided the accumulation of waste residue waste material, the waste residue waste material is all removed totally at every turn, can not solidify, spoil disposal is natural and tripping, the raising factor of created gase satisfactory for result of spoil disposal.
4. the application of various valves reaches the applying in a flexible way of equipment on the one hand in the utility model, on the other hand, the also flow direction of controlled liq admirably, the waste residue waste material blocking pipeline of anti-backflow influences cleaning performance.
5. the device of the utility model design adopts the supernatant liquor in the reactor to wash, and has not only saved resource greatly, and because liquid circulates in system, has avoided liquid to flow out the valuable gases dissipation that causes inevitably, and is convenient and practical, energy-conserving and environment-protective.
Description of drawings
Fig. 1 is the structural representation of the utility model soil discharging facility embodiment 1
Fig. 2 is the cross-sectional structure synoptic diagram of the utility model soil discharging facility embodiment 1
Fig. 3 is Figure 1A part structure for amplifying synoptic diagram of the utility model soil discharging facility
1 reactor, 2 water body primary input pipelines, 3 water body output channels, 4 water bodys divide output channel 5 water body spargers 6 reverse checkvalves 7 stopping valve 8 gate valves 9 flushing pumps 10 elbows 11 supernatant liquors 12 gate valves
Embodiment
Below in conjunction with drawings and Examples the utility model is further specified, but not as to qualification of the present utility model.
See also the embodiment of the utility model soil discharging facility shown in Fig. 1-3.
Embodiment 1
With the soil discharging facility that reactor 1 is connected, comprise that Controlling System, flushing pump, water body primary input pipeline, water body sparger, water body divide output channel, gate valve; Described Controlling System is connected by electrical signal with flushing pump, gate valve, reverse checkvalve; Described water body sparger is positioned at reactor 1, the bottom position intermediate; Flushing pump is connected with reactor 1 top by water body primary input pipeline, and flushing pump is connected with the water body sparger by water body master output channel; Described gate valve is positioned on the water body primary input pipeline of ingress of flushing pump, and on the water body master output channel in exit.Described water body divides output channel to be connected with the water body sparger.
Also comprise stopping valve, reverse checkvalve, described stopping valve 7 is positioned at the part of water body master output channel near flushing pump; Reverse checkvalve 6 is positioned at the exit that water body primary input pipeline, water body master output channel and water body divide output channel.
The inlet of described flushing pump communicates with the supernatant layer place on reactor 1 top by water body primary input pipeline, and described flushing pump outlet is connected with the water body sparger by water body master output channel;
Described Controlling System comprises power distribution cabinet, control panel, and power distribution cabinet is connected by electrical signal with control panel; Described electrical signal transmits by the electric wire transmission or by wireless device, preferred wire equipment.
The inlet of described flushing pump, outlet all communicate with reactor 1 through pipeline; On the pipeline of the ingress of flushing pump gate valve is housed, on the pipeline in exit gate valve is housed, the gate valve role is for controlling flushing pump neatly.
Supernatant layer place in the inlet of described flushing pump and the reactor 1 communicates; Described flushing pump outlet communicates with the water body output channel, and the water body output channel communicates with the water body sparger; Described water body sparger divides output channel to communicate with water body, and control valve all is housed, to control the switching at the place that respectively communicates.
Divide the outlet of output channel to be equipped with elbow at described each water body, by elbow straight current are become the current with angle, current just can make the current of flushing form the whirlpool shape after having certain angle, could wash thoroughly, bend angle α is 30 °, the bending direction unanimity of elbow, all crooked in the counterclockwise direction.
Reverse checkvalve all is equipped with in the exit of described each hydraulic pipe, avoids liquid to produce backflow phenomenon pollution and obstruction water pipe under the effect of pressure.
It is two or more that water body divides output channel, is the center with the water body sparger, evenly distributed.
Water body divides preferred 6 of output channel, is the center with the water body sparger, and it is 60 ° that evenly distributed each water body divides the angle between the output channel.
Embodiment 2
The bending of described elbow clockwise direction, bend angle α is 35 degree, it is eight that water body divides output channel, is the center with the water body sparger, evenly distributed.All the other are with embodiment 1.
The bending of described elbow clockwise direction, bend angle α is 25 degree, it is four that water body divides output channel, is the center with the water body sparger, evenly distributed.All the other are with embodiment 1.
Above-described embodiment, the utility model embodiment a kind of more preferably just, the common variation that those skilled in the art carries out in the technical solutions of the utility model scope and replacing all should be included in the protection domain of the present utility model.
Claims (10)
1. a soil discharging facility is connected with reactor, it is characterized in that, comprises that Controlling System, flushing pump, water body primary input pipeline, water body master output channel, water body sparger, water body divide output channel, gate valve; Described Controlling System is connected by electrical signal with flushing pump, gate valve; Described water body sparger is positioned at reactor, the bottom position intermediate; Flushing pump is connected with reactor top by water body primary input pipeline, and flushing pump is connected with the water body sparger by water body master output channel; Described gate valve is positioned on the water body primary input pipeline of ingress of flushing pump, and on the water body master output channel in exit; Described water body divides output channel to be connected with the water body sparger.
2. soil discharging facility according to claim 1 is characterized in that: also comprise stopping valve, reverse checkvalve, described stopping valve 7 is positioned at the part of water body master output channel near flushing pump; Described reverse checkvalve is positioned at the exit that water body primary input pipeline, water body master output channel and water body divide output channel; Stopping valve all is connected with Controlling System by electrical signal with reverse checkvalve.
3. soil discharging facility according to claim 1 is characterized in that: the inlet of described flushing pump communicates with the supernatant layer place on reactor top by water body primary input pipeline, and described flushing pump outlet is connected with the water body sparger by the water body output channel;
4. soil discharging facility according to claim 1 is characterized in that: described Controlling System comprises power distribution cabinet, control panel, and control panel is connected with power distribution cabinet by electrical signal.
5. soil discharging facility according to claim 1 is characterized in that: also comprise elbow, described elbow is positioned at the outlet that water body divides output channel, and bend angle α is 10-80 °.
6. soil discharging facility according to claim 5 is characterized in that: bend angle α is 15-45 °.
7. soil discharging facility according to claim 5 is characterized in that: bend angle α is 25-35 °.
8. soil discharging facility according to claim 5 is characterized in that: bend angle α is 30 °.
9. soil discharging facility according to claim 1 is characterized in that: it is two or more that water body divides output channel, is the center with the water body sparger, evenly distributed.
10. soil discharging facility according to claim 9 is characterized in that: it is 6 that water body divides output channel, is the center with the water body sparger, evenly distributed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202199813U CN201581072U (en) | 2009-10-23 | 2009-10-23 | Sludge discharge device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009202199813U CN201581072U (en) | 2009-10-23 | 2009-10-23 | Sludge discharge device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201581072U true CN201581072U (en) | 2010-09-15 |
Family
ID=42723070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009202199813U Expired - Fee Related CN201581072U (en) | 2009-10-23 | 2009-10-23 | Sludge discharge device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201581072U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102628016A (en) * | 2011-08-18 | 2012-08-08 | 舒方银 | Totally enclosed water-gas linkage intermittent internal rotation anaerobic digestion device with constant temperature for house refuse |
| CN105199947A (en) * | 2015-09-23 | 2015-12-30 | 许显国 | Split type vortex methane breathing machine |
| CN105199946A (en) * | 2015-09-23 | 2015-12-30 | 许显国 | Vortex marsh gas breathing machine |
-
2009
- 2009-10-23 CN CN2009202199813U patent/CN201581072U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102628016A (en) * | 2011-08-18 | 2012-08-08 | 舒方银 | Totally enclosed water-gas linkage intermittent internal rotation anaerobic digestion device with constant temperature for house refuse |
| CN102628016B (en) * | 2011-08-18 | 2014-04-16 | 舒方银 | Totally enclosed water-gas linkage intermittent internal rotation anaerobic digestion device with constant temperature for house refuse |
| CN105199947A (en) * | 2015-09-23 | 2015-12-30 | 许显国 | Split type vortex methane breathing machine |
| CN105199946A (en) * | 2015-09-23 | 2015-12-30 | 许显国 | Vortex marsh gas breathing machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201581072U (en) | Sludge discharge device | |
| CN105152508A (en) | Reinforced sludge anaerobic fermentation device | |
| CN202786235U (en) | Circulation biogas slurry pipeline for biogas slurry stirring and hull breaking of anaerobic reactor | |
| CN104402114B (en) | Acidication waste disposal plant | |
| CN203545784U (en) | Combined type oxidation ditch with external sedimentation basin | |
| CN103241834B (en) | Pulse internal circulation anaerobic reactor | |
| CN202022925U (en) | Device for pressurizing, backflowing, shell breaking and stirring methane liquid at bottom layer of methane tank | |
| CN202063776U (en) | Improved three-compartment type septic tank | |
| CN208104025U (en) | A kind of anaerobic reactor | |
| CN206089192U (en) | Upflow anaerobic sludge bed reaction unit | |
| CN206562331U (en) | A kind of hydrolysis acidification pool | |
| CN206069510U (en) | A kind of sewage treatment anaerobic reactor | |
| CN204369652U (en) | A kind of complete hybrid anaerobic system for landfill leachate treatment | |
| CN201082875Y (en) | Energy-saving impulse anaerobic reactor | |
| CN204752312U (en) | Up -flow anaerobic sludge blanket filtering pond | |
| CN201330195Y (en) | EGSB integrated reactor | |
| CN211284352U (en) | Complementary stirring full-mixing anaerobic reactor | |
| CN102515340A (en) | Upper-flow sequencing batch methane tank | |
| CN202499758U (en) | Efficient precipitation/return anaerobic fermentation reactor | |
| CN203794697U (en) | Novel hydrolytic acidification reinforcing reaction device | |
| CN202072579U (en) | Automatic sludge discharging device | |
| CN205953651U (en) | Fast anaerobic reactor of multistage unsteady flow | |
| CN202400903U (en) | Integrated hydrolyzing and acidizing device for pharmaceutical wastewater treatment | |
| CN205773614U (en) | A kind of novel hydrolysis and acidification treater | |
| CN204455090U (en) | Hydraulic mixing anaerobic jar |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20100915 Termination date: 20151023 |
|
| EXPY | Termination of patent right or utility model |