CN106390548A - Continuous biogas slurry filtering device and method - Google Patents
Continuous biogas slurry filtering device and method Download PDFInfo
- Publication number
- CN106390548A CN106390548A CN201611054496.6A CN201611054496A CN106390548A CN 106390548 A CN106390548 A CN 106390548A CN 201611054496 A CN201611054496 A CN 201611054496A CN 106390548 A CN106390548 A CN 106390548A
- Authority
- CN
- China
- Prior art keywords
- biogas slurry
- biogas
- screen pack
- stoste
- filter
- 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.)
- Pending
Links
- 239000002002 slurry Substances 0.000 title claims abstract description 178
- 238000001914 filtration Methods 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 18
- 239000002893 slag Substances 0.000 claims description 26
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 22
- 230000003028 elevating effect Effects 0.000 claims description 19
- 238000004140 cleaning Methods 0.000 claims description 12
- 239000000377 silicon dioxide Substances 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 10
- 230000000903 blocking effect Effects 0.000 claims description 6
- 238000011065 in-situ storage Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 230000001419 dependent effect Effects 0.000 claims description 3
- 230000008021 deposition Effects 0.000 claims description 3
- 239000013049 sediment Substances 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 238000007667 floating Methods 0.000 claims description 2
- 206010020112 Hirsutism Diseases 0.000 claims 1
- 239000000706 filtrate Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 8
- 238000000926 separation method Methods 0.000 abstract description 7
- 239000012535 impurity Substances 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 239000010815 organic waste Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000004744 fabric Substances 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000007850 degeneration Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000686 essence Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 244000144972 livestock Species 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
- B01D29/606—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration by pressure measuring
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/64—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element
- B01D29/6407—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element brushes
- B01D29/6423—Regenerating the filter material in the filter by scrapers, brushes, nozzles, or the like, acting on the cake side of the filtering element brushes with a translational movement with respect to the filtering element
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
The invention relates to a continuous biogas slurry filtering device and method. The continuous biogas slurry filtering device structurally mainly comprises a biogas slurry filtering device casing and a filter net in the casing, wherein the filter net divides the casing into two parts, namely, an original biogas slurry chamber on the left of the filter net and a filtered biogas slurry chamber on the right of the filter net in the casing; a biogas slurry input pipe is arranged at the upper part of the original biogas slurry chamber side, and a residue discharge pipe is arranged at the bottom; a biogas slurry output pipe is arranged at the bottom of the filtered biogas slurry chamber; an elongated scraper, a residue outlet and a residue outlet cover plate are arranged in the original biogas slurry chamber, a brush is inlaid on one side, contacted with the filter net, of the scraper, and the top end of the scraper and the residue outlet cover plate are both connected with a movable lifting rod. The device is simple in structure and convenient to operate, the biogas slurry filtering effect that biogas residues, impurities and dross in biogas slurry are removed simultaneously is realized, a screen is cleaned on site, online residue discharge is realized, and the continuity and high efficiency of solid-liquid separation of the biogas slurry are guaranteed.
Description
Technical field
The present invention relates to agriculture and forestry organic waste material recycling and biogas engineering biogas residue and biogas liquid separation technology field and in particular to
A kind of continous way biogas slurry filter and method.
Technical background
Biogas slurry, as the product of the fermentation such as agricultural organic waste, feces of livestock and poultry, domestic organic garbage, price is low
Honest and clean, wide material sources, its internal component is rich in compared with multi-nutrient element, degeneration-resistant, sterilization component and crop growth accelerant, is to grind at present
Study carefully the popular green organic fertilizer of comparison.Because the fermented rear biogas slurry being formed is tasteless, fertilizer efficiency often general chemistry synthesis again
More than 10 times of fertilizer, and water quality characteristic is also easily absorbed by crops, so biogas slurry has in agriculture and forestry organic waste material recycling
The prospect of being widely applied.
But due to often containing more biogas residue, impurity and scum silica frost in biogas slurry, easily block in sprinkling irrigation application
Shower nozzle, leads to spraying effect not good, makes the application of biogas slurry be subject to more serious restricting with promoting.Biogas slurry filters, and is to solve this
One of important method of one problem.Biogas slurry filter common at present, is carried out using sieve method or extruding filtration method mostly
Separation of solid and liquid is realizing the filtration of biogas slurry.Because the biogas residue in biogas slurry and stalk crude fibre are easy to block mesh screen, need the cycle
Property ground stop the work of biogas slurry filtration separation, dismounting cleaning screen pack of offing normal realizing the recycling of screen pack, to ensure biogas slurry
That filters proceeds.Additionally, the biogas residue after biogas slurry filtration, when slagging tap, also tend to need to stop biogas slurry filtration work to enter
Row is slagged tap.These discontinuous biogas slurry filter methods, not only affect persistently carrying out of biogas slurry filtration work, and maintenance of clean-up are not
Just, it is higher that the equipment being related to also tends to complex structure, cost.Seek a kind of structure be simple and convenient to operate, cheap biogas slurry
Filter and method, it appears particularly important.
Content of the invention
It is an object of the invention to overcoming above-mentioned deficiency, provide a kind of continous way biogas slurry filter and method, between not
Realize biogas residue, the separation of biogas slurry under conditions of disconnected work and clear up screen cloth in situ, slag tap online, structure is simple, easy to operate.
The know-why of the present invention：
Biogas slurry filter housing is divided into biogas slurry stoste room and filtered fluid by screen pack by a kind of continous way biogas slurry filter
Room；Biogas slurry filters and occurs mainly in biogas slurry stoste room, flows into indoor biogas slurry stoste through biogas slurry input pipe, because volume expands
Greatly, flow velocity reduces, and wherein the larger biogas residue of weight and other impurities sink to room bottom, and the scum silica frost of lighter weight is then cut by screen pack
Stay in biogas slurry stoste room, biogas slurry then passes through filter screen to reach biogas slurry filtered fluid room, realizes the filtration of biogas slurry.With filtration time
Increase, in order to prevent gradually increasing and block screen pack because sticking to the scum silica frost on screen pack, using being connected with movable elevating lever
The strip scraper plate with hairbrush clean screen pack with water it is achieved that to the cleaning of the original position of sieve aperture it is ensured that natural pond during cleaning screen pack
What liquid filtered is normally carried out；And the biogas residue of biogas slurry stoste room bottom then passes through slag notch, and the scum pipe through bottom is timed
Discharge cleaning；Slagging tap velar plate in biogas slurry stoste room, is connected with movable elevating lever, and when filtering at ordinary times, cover plate is located at biogas slurry stoste room
Top, when slagging tap, cover plate drops under the drive of movable elevating lever and covers slag notch, make to slag tap and stoste filter every
Open it is ensured that when slagging tap biogas slurry filter be normally carried out.In situ cleaning screen pack with slag tap it is ensured that the company filtered of biogas slurry in situ
Continuous property is carried out.
Technical scheme：
A kind of continous way biogas slurry filter, including the screen pack of biogas slurry filter housing and Qi Nei, described screen pack is by institute
State housing and be divided into two parts, housing filtering net is divided into biogas slurry stoste room with left part, biogas slurry filtered fluid room is divided into right part；Described
Biogas slurry stoste room upper lateral part is provided with biogas slurry input pipe, and bottom is provided with scum pipe；
Described biogas slurry filtered fluid room bottom is provided with biogas slurry efferent duct；
Described biogas slurry stoste is indoor, is provided with strip scraper plate, and the one side that scraper plate contacts with filter screen is inlaid with hairbrush, scraper plate top and
Movable elevating lever is connected；
Described biogas slurry stoste is indoor, is provided with slag notch and velar plate of slagging tap, described velar plate of slagging tap is connected with movable elevating lever；
On described biogas slurry input pipe, efferent duct and scum pipe, it is equipped with valve；
It is equipped with pressure gauge on described biogas slurry input pipe, efferent duct；
Preferably, the mesh screen of described screen pack is 80-100 mesh；
Preferably, described screen pack is stainless (steel) wire；
Preferably, described movable elevating lever is connected with cylinder；
Preferably, described strip blade height and screen pack aspect ratio are 1/8-1/5；
A kind of method carrying out biogas slurry filtration using described continous way biogas slurry filter, comprises the following steps：
（1）Biogas slurry filters
The biogas slurry input valve of the continous way biogas slurry filter as described in technical scheme and output end valve are all opened, row
Slag end valve closing, velar plate of slagging tap rises to biogas slurry stoste ceiling end；Biogas slurry stoste flows into described natural pond from described biogas slurry input pipe
Liquid stoste room, after sediment, filtration, reaches described biogas slurry filtered fluid room, and through the output of described biogas slurry efferent duct；
（2）Screen pack is cleared up in situ
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, stick to floating on screen pack
Slag gradually increases, and for preventing scum silica frost from blocking described screen pack, regularly enables the strip scraper plate with hairbrush, is not removing described mistake
In the case of filter screen, so that described scraper plate is done under the drive of movable elevating lever, to move in parallel friction back and forth up and down described to clean with water
Screen pack, makes the scum silica frost of adhesion come off from described screen pack, realizes the original position cleaning of screen pack；
（3）Biogas residue is slagged tap online
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, heavier biogas residue is deposited on institute
State the bottom of biogas slurry stoste room, before biogas residue deposition height exceedes described slag notch, will be movable with what velar plate of slagging tap was connected
Elevating lever declines, till described cover plate covers completely and compresses described slag notch；Now, described biogas slurry input valve and
Output end valve is still in opening, and described velar plate of slagging tap makes biogas slurry stoste with the natural pond of described biogas slurry stoste room bottom
Slag separates；Open described slag output end valve so that it may not interrupt carrying out slagging tap online of biogas residue in the case that biogas slurry filters；
Above-mentioned steps（1）In, when normal biogas slurry filters operating mode, described biogas slurry input pressure gauge exports side pressure with described biogas slurry
Pressure difference value between power table should be less than 0.3Mpa；When described biogas slurry input pressure gauge and described biogas slurry delivery guage it
Between pressure difference value be more than 0.3Mpa when, show that described continous way biogas slurry filter blocks, need cleaning, now need
Execution above-mentioned steps（2）；Pressure difference value between described biogas slurry input pressure gauge and biogas slurry delivery guage is less than
During 0.05MPa, illustrate that the blocking material on described screen pack has been cleaned out, can be normally carried out filtering work；
Above-mentioned steps（3）, can follows step（2）Execution, also dependent on needs, individually executes.
Beneficial effects of the present invention：
（1）Present invention achieves remove the comprehensive filter effect of biogas slurry of the biogas residue, impurity and scum silica frost in biogas slurry simultaneously；
（2）Present invention achieves the original position cleaning of screen pack, it is to avoid because needing the cycle in existing most of biogas slurry filtering techniques
Property off normal cleaning or change screen cloth and lead to separation of solid and liquid work interruption；Meanwhile, present invention achieves biogas residue online
Slag tap, further ensure the continuity of biogas slurry separation of solid and liquid work；
（3）Present configuration is simple, easy to operate, effectively achieves the filtration of biogas slurry and the deslagging of biogas residue.
Brief description
Fig. 1 is a kind of structural representation of continous way biogas slurry filter of the present invention.
In figure：1. biogas slurry filter housing, 2. screen pack, 3. movable elevating lever, 4. biogas slurry input pipe, 5. biogas slurry is defeated
Enter end pressure table, 6. biogas slurry input valve, 7. scum pipe, 8. deslagging end valve door, 9. slag notch, 10. it is inlaid with the length of hairbrush
Bar shaped scraper plate, 11. biogas slurry efferent ducts, 12. biogas slurry delivery guages, 13. biogas slurry output end valves, 14. movable elevating levers,
15. slag tap velar plate.
Specific embodiment
Below in conjunction with the accompanying drawings further detailed description is done to the present invention, but embodiments of the present invention not limited to this.
Embodiment one：
A kind of continous way biogas slurry filter, including the screen pack 2 of biogas slurry filter housing 1 and Qi Nei, described screen pack 2 will
Described housing 1 is divided into two parts, and housing filtering net 2 is divided into biogas slurry stoste room with left part, is divided into biogas slurry filtered fluid room with right part；
Described biogas slurry stoste room upper lateral part is provided with biogas slurry input pipe 4, and bottom is provided with scum pipe 7；
Described biogas slurry filtered fluid room bottom is provided with biogas slurry efferent duct 11；
Described biogas slurry stoste is indoor, is provided with strip scraper plate 10, the one side that scraper plate 10 is contacted with filter screen 2 is inlaid with hairbrush, scraper plate
Top is connected with movable elevating lever 3；
Described biogas slurry stoste is indoor, is provided with slag notch 9 and velar plate 15 of slagging tap, described velar plate 9 and the movable elevating lever of slagging tap
14 are connected；
On described biogas slurry input pipe 4, efferent duct 11 and scum pipe 7, it is equipped with valve；
On described biogas slurry input pipe 4, efferent duct 11, it is equipped with pressure gauge；
Preferably, the mesh screen of described screen pack 2 is 80-100 mesh；
Preferably, described screen pack 2 is stainless (steel) wire；
Preferably, described movable elevating lever connects 3 and 14, it is respectively connected with cylinder；
Preferably, the height of described strip scraper plate 10 is 1/8-1/5 with the aspect ratio of screen pack 2；
Embodiment two：
A kind of method carrying out biogas slurry filtration using continous way biogas slurry filter described in embodiment one：
（1）Biogas slurry filters
The biogas slurry input valve 6 of the continous way biogas slurry filter as described in technical scheme and output end valve 13 are all beaten
Open, deslagging end valve door 8 is closed, velar plate 15 of slagging tap rises to biogas slurry stoste ceiling end；Biogas slurry stoste flows from described biogas slurry input pipe 4
Enter described biogas slurry stoste room, after sediment, filtration, reach described biogas slurry filtered fluid room, and export through described biogas slurry efferent duct 11；
（2）Screen pack is cleared up in situ
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, stick on screen pack 2
Scum silica frost gradually increases, and for preventing scum silica frost from blocking described screen pack 2, regularly enables the strip scraper plate 10 with hairbrush, is not removing
In the case of described screen pack 2, so that described scraper plate 10 is done under the drive of movable elevating lever 3 and move in parallel friction back and forth up and down
To clean described screen pack 2 with water, so that the scum silica frost of adhesion is come off from described screen pack 2, to realize the original position cleaning of screen pack；
（3）Biogas residue is slagged tap online
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, heavier biogas residue is deposited on institute
State the bottom of biogas slurry stoste room, biogas residue deposition height exceed described slag notch before, by with living that velar plate 15 of slagging tap is connected
Dynamic elevating lever 14 declines, till described cover plate covers completely and compresses described slag notch 9；Now, described biogas slurry input
Valve 6 and output end valve 13 are still in opening, and described velar plate 15 of slagging tap makes biogas slurry stoste former with described biogas slurry
The biogas residue of liquid room bottom separates；Open described slag output end valve 8 so that it may not interrupt carrying out biogas residue in the case that biogas slurry filters
Slag tap online；
Above-mentioned steps（1）In, when normal biogas slurry filters operating mode, described biogas slurry input pressure gauge 5 and described biogas slurry output end
Pressure difference value between pressure gauge 12 should be less than 0.3Mpa；When described biogas slurry input pressure gauge 5 and described biogas slurry export side pressure
When pressure difference value between power table 12 is more than 0.3Mpa, show that described continous way biogas slurry filter blocks, need to clear up,
Now need to execute above-mentioned steps（2）；Pressure between described biogas slurry input pressure gauge 5 and biogas slurry delivery guage 12
When difference is less than 0.05MPa, illustrates that the blocking material on described screen pack 2 has been cleaned out, filterer can be normally carried out
Make；
Above-mentioned steps（3）, can follows step（2）Execution, also dependent on needs, individually executes.
Above-described embodiment is the present invention preferably embodiment, but embodiments of the present invention are not subject to above-described embodiment
Limit, other any Spirit Essences without departing from the present invention and the change made under principle, modification, replacement, combine, simplify,
All should be equivalent substitute mode, be included within protection scope of the present invention.
Claims (5)
1. a kind of continous way biogas slurry filter it is characterised in that：Described device includes biogas slurry filter housing and Qi Nei's
Screen pack, described housing is divided into two parts by described screen pack, and housing filtering net is divided into biogas slurry stoste room with left part, with right part
It is divided into biogas slurry filtered fluid room；Described biogas slurry stoste room upper lateral part is provided with biogas slurry input pipe, and bottom is provided with scum pipe；Described biogas slurry mistake
Filtrate chamber bottom is provided with biogas slurry efferent duct.
2. a kind of continous way biogas slurry filter according to claim 1 it is characterised in that：Described biogas slurry stoste interior sets
There are strip scraper plate, slag notch and velar plate of slagging tap, the one side that described strip scraper plate is contacted with described screen pack inlays hairiness
Brush；Described strip scraper plate top and described velar plate of slagging tap, are all connected with movable elevating lever.
3. a kind of continous way biogas slurry filter according to claim 1 it is characterised in that：Described biogas slurry input pipe, defeated
In outlet pipe and scum pipe, it is equipped with valve；It is equipped with pressure gauge on described biogas slurry input pipe, efferent duct.
4. a kind of continous way biogas slurry filter according to claim 1 it is characterised in that：The mesh screen of described screen pack is
The stainless (steel) wire of 80 mesh～100 mesh；Described movable elevating lever is connected with cylinder；Described strip blade height and described filtration
Net height is than for 1/8～1/5.
5. using a kind of continous way biogas slurry filter described in claim 1 carry out biogas slurry filtration method it is characterised in that
Comprise the following steps：
（1）Biogas slurry filters
The biogas slurry input valve of continous way biogas slurry filter as claimed in claim 1 and output end valve are all opened,
Deslagging end valve closing, velar plate of slagging tap rises to biogas slurry stoste ceiling end；Biogas slurry stoste flows into described from described biogas slurry input pipe
Biogas slurry stoste room, after sediment, filtration, reaches described biogas slurry filtered fluid room, and through the output of described biogas slurry efferent duct；
（2）Screen pack is cleared up in situ
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, stick to floating on screen pack
Slag gradually increases, and for preventing scum silica frost from blocking described screen pack, regularly enables the strip scraper plate with hairbrush, is not removing described mistake
In the case of filter screen, so that described scraper plate is done under the drive of movable elevating lever, to move in parallel friction back and forth up and down described to clean with water
Screen pack, makes the scum silica frost of adhesion come off from described screen pack, realizes the original position cleaning of screen pack；
（3）Biogas residue is slagged tap online
In such as above-mentioned steps（1）In described biogas slurry filter process, with the growth of filtration time, heavier biogas residue is deposited on institute
State the bottom of biogas slurry stoste room, before biogas residue deposition height exceedes described slag notch, will be movable with what velar plate of slagging tap was connected
Elevating lever declines, till described cover plate covers completely and compresses described slag notch；Now, described biogas slurry input valve and
Output end valve is still in opening, and described velar plate of slagging tap makes biogas slurry stoste with the natural pond of described biogas slurry stoste room bottom
Slag separates；Open described slag output end valve so that it may not interrupt carrying out slagging tap online of biogas residue in the case that biogas slurry filters；
Above-mentioned steps（1）In, when normal biogas slurry filters operating mode, described biogas slurry input pressure gauge exports side pressure with described biogas slurry
Pressure difference value between power table should be less than 0.3Mpa；When described biogas slurry input pressure gauge and described biogas slurry delivery guage it
Between pressure difference value be more than 0.3Mpa when, show that described continous way biogas slurry filter blocks, need cleaning, now need
Execution above-mentioned steps（2）；Pressure difference value between described biogas slurry input pressure gauge and biogas slurry delivery guage is less than
During 0.05MPa, illustrate that the blocking material on described screen pack has been cleaned out, can be normally carried out filtering work；Above-mentioned step
Suddenly（3）, can follows step（2）Execution, also dependent on needs, individually executes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611054496.6A CN106390548A (en) | 2016-11-25 | 2016-11-25 | Continuous biogas slurry filtering device and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611054496.6A CN106390548A (en) | 2016-11-25 | 2016-11-25 | Continuous biogas slurry filtering device and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106390548A true CN106390548A (en) | 2017-02-15 |
Family
ID=58081606
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611054496.6A Pending CN106390548A (en) | 2016-11-25 | 2016-11-25 | Continuous biogas slurry filtering device and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106390548A (en) |
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715625A (en) * | 2017-10-09 | 2018-02-23 | 天津水天大周科技有限公司 | A kind of novel deduster |
| CN107974398A (en) * | 2017-12-26 | 2018-05-01 | 中国农业科学院农业资源与农业区划研究所 | A kind of High-efficiency straw is degradable fermented and biogas slurry multistage filtering cyclic utilization system device |
| CN108176097A (en) * | 2017-12-26 | 2018-06-19 | 中国农业科学院农业资源与农业区划研究所 | Integrated device is applied in a kind of biogas slurry filtering |
| CN108211469A (en) * | 2018-01-05 | 2018-06-29 | 惠安北酷机械科技有限公司 | Juice residue High-cfficiency Filtration equipment in a kind of sugar processing raw material |
| CN108295527A (en) * | 2018-01-24 | 2018-07-20 | 庄燕双 | A kind of Domestic waster water treater |
| CN109724840A (en) * | 2019-02-08 | 2019-05-07 | 桐乡市麦西微服饰有限公司 | A kind of detection sea surface water extraction device and operating method |
| CN110201437A (en) * | 2019-05-08 | 2019-09-06 | 天津市亨必达化学合成物有限公司 | Novel pharmaceutical purpose wastewater filtering device |
| CN117414798A (en) * | 2023-12-19 | 2024-01-19 | 成都赢纳环保科技有限公司 | Reation kettle that environment-friendly medicament production was used |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005095743A (en) * | 2003-09-24 | 2005-04-14 | Sumitomo Chemical Co Ltd | Solid-liquid separation device and solid-liquid separation method |
| CN101564611A (en) * | 2009-06-05 | 2009-10-28 | 中国农业科学院蔬菜花卉研究所 | Marsh liquid filter |
| CN201366269Y (en) * | 2009-01-12 | 2009-12-23 | 罗成 | On-line decontamination and cleaning filter with two-stage filtering function |
| CN203492375U (en) * | 2013-08-05 | 2014-03-26 | 雷经洋 | Environment-friendly fertilizer fertilizing irrigation device |
| CN104436822A (en) * | 2014-12-18 | 2015-03-25 | 天津泽昌化工设备制造有限公司 | Self-cleaning horizontal type dirt remover |
| CN104641777A (en) * | 2013-11-20 | 2015-05-27 | 江柏田 | Field biogas slurry fertilization integrated irrigating system |
| CN204543693U (en) * | 2015-03-27 | 2015-08-12 | 优思克（北京）生物能源科技有限公司 | A kind of natural pond liquid filter |
| CN205443278U (en) * | 2016-03-29 | 2016-08-10 | 宿迁市环宇牧业有限公司 | Grow cyclic utilization device of discarded object |
| CN205516720U (en) * | 2016-01-28 | 2016-08-31 | 成都市农林科学院 | Natural pond liquid filter equipment |
| CN206366233U (en) * | 2016-11-25 | 2017-08-01 | 西北农林科技大学 | A kind of continous way biogas slurry filter |
-
2016
- 2016-11-25 CN CN201611054496.6A patent/CN106390548A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005095743A (en) * | 2003-09-24 | 2005-04-14 | Sumitomo Chemical Co Ltd | Solid-liquid separation device and solid-liquid separation method |
| CN201366269Y (en) * | 2009-01-12 | 2009-12-23 | 罗成 | On-line decontamination and cleaning filter with two-stage filtering function |
| CN101564611A (en) * | 2009-06-05 | 2009-10-28 | 中国农业科学院蔬菜花卉研究所 | Marsh liquid filter |
| CN203492375U (en) * | 2013-08-05 | 2014-03-26 | 雷经洋 | Environment-friendly fertilizer fertilizing irrigation device |
| CN104641777A (en) * | 2013-11-20 | 2015-05-27 | 江柏田 | Field biogas slurry fertilization integrated irrigating system |
| CN104436822A (en) * | 2014-12-18 | 2015-03-25 | 天津泽昌化工设备制造有限公司 | Self-cleaning horizontal type dirt remover |
| CN204543693U (en) * | 2015-03-27 | 2015-08-12 | 优思克（北京）生物能源科技有限公司 | A kind of natural pond liquid filter |
| CN205516720U (en) * | 2016-01-28 | 2016-08-31 | 成都市农林科学院 | Natural pond liquid filter equipment |
| CN205443278U (en) * | 2016-03-29 | 2016-08-10 | 宿迁市环宇牧业有限公司 | Grow cyclic utilization device of discarded object |
| CN206366233U (en) * | 2016-11-25 | 2017-08-01 | 西北农林科技大学 | A kind of continous way biogas slurry filter |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107715625A (en) * | 2017-10-09 | 2018-02-23 | 天津水天大周科技有限公司 | A kind of novel deduster |
| CN107974398A (en) * | 2017-12-26 | 2018-05-01 | 中国农业科学院农业资源与农业区划研究所 | A kind of High-efficiency straw is degradable fermented and biogas slurry multistage filtering cyclic utilization system device |
| CN108176097A (en) * | 2017-12-26 | 2018-06-19 | 中国农业科学院农业资源与农业区划研究所 | Integrated device is applied in a kind of biogas slurry filtering |
| CN107974398B (en) * | 2017-12-26 | 2023-11-03 | 中国农业科学院农业资源与农业区划研究所 | Straw efficient degradation fermentation and biogas slurry multistage filtration recycling system device |
| CN108211469A (en) * | 2018-01-05 | 2018-06-29 | 惠安北酷机械科技有限公司 | Juice residue High-cfficiency Filtration equipment in a kind of sugar processing raw material |
| CN108295527A (en) * | 2018-01-24 | 2018-07-20 | 庄燕双 | A kind of Domestic waster water treater |
| CN109724840A (en) * | 2019-02-08 | 2019-05-07 | 桐乡市麦西微服饰有限公司 | A kind of detection sea surface water extraction device and operating method |
| CN109724840B (en) * | 2019-02-08 | 2021-07-23 | 广州海兰图检测技术有限公司 | Ocean surface water extraction device for detection and operation method |
| CN110201437A (en) * | 2019-05-08 | 2019-09-06 | 天津市亨必达化学合成物有限公司 | Novel pharmaceutical purpose wastewater filtering device |
| CN117414798A (en) * | 2023-12-19 | 2024-01-19 | 成都赢纳环保科技有限公司 | Reation kettle that environment-friendly medicament production was used |
| CN117414798B (en) * | 2023-12-19 | 2024-04-05 | 成都赢纳环保科技有限公司 | Reation kettle that environment-friendly medicament production was used |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106390548A (en) | Continuous biogas slurry filtering device and method | |
| CN106943781A (en) | A kind of pulling flow type biogas slurry and biogas residue separator | |
| CN206777964U (en) | A kind of automatically cleaning honey filter device | |
| CN201168484Y (en) | Sprinkler drip irrigation filter | |
| CN208694441U (en) | A kind of biogas slurry collection device having filtering function | |
| CN209178354U (en) | A kind of purifier of camellia seed oil | |
| CN206366233U (en) | A kind of continous way biogas slurry filter | |
| CN204543693U (en) | A kind of natural pond liquid filter | |
| CN206284142U (en) | One kind can the self-clearing high-density fish culture pool | |
| CN104831778A (en) | Rainwater storage and utilization device | |
| CN208212631U (en) | A kind of sewage filtration equipment | |
| CN206587480U (en) | Automatic discharge efficient decolorizing regenerates oil conditioner | |
| CN211799350U (en) | Camellia oil filter equipment | |
| CN110810206A (en) | Energy-conserving irrigation equipment of afforestation with sewage recovery stage filtering capability | |
| CN207478140U (en) | A kind of filter plant for being used to prepare watermelon ketone | |
| CN221887328U (en) | Ponding device for recovering degraded vegetation in desert area | |
| CN106186109A (en) | A kind of grid pond Nicotiana tabacum L. wastewater suspended substance collects separate tank | |
| CN206229005U (en) | A kind of high-efficiency environment friendly biogas slurry filter | |
| CN220309885U (en) | Water circulation mechanism for tomato breeding | |
| CN204469382U (en) | Sandrock filter | |
| CN109794099A (en) | A kind of agricultural cultivation drop irrigation filtering device | |
| CN204699486U (en) | A kind of Full-automatic self-cleaning filter | |
| CN204865204U (en) | Dual fail -safe formula filter | |
| CN215137429U (en) | Fruit tree is irrigated and is used high-efficient water filtering ponds | |
| CN203814399U (en) | Combined pollution discharge device applicable to bottom discharger blockage prevention of circulating water loach culture pool |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170215 |
|
| WD01 | Invention patent application deemed withdrawn after publication |