CN206045549U - Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put - Google Patents
Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put Download PDFInfo
- Publication number
- CN206045549U CN206045549U CN201621082211.5U CN201621082211U CN206045549U CN 206045549 U CN206045549 U CN 206045549U CN 201621082211 U CN201621082211 U CN 201621082211U CN 206045549 U CN206045549 U CN 206045549U
- Authority
- CN
- China
- Prior art keywords
- strainer
- impurity
- liquid
- mummification
- liquid impurity
- 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.)
- Active
Links
- 239000012535 impurity Substances 0.000 title claims abstract description 187
- 239000007788 liquid Substances 0.000 title claims abstract description 173
- 230000018044 dehydration Effects 0.000 title claims abstract description 38
- 238000006297 dehydration reaction Methods 0.000 title claims abstract description 38
- 230000007246 mechanism Effects 0.000 claims abstract description 66
- 230000014759 maintenance of location Effects 0.000 claims abstract description 15
- 239000012141 concentrate Substances 0.000 claims abstract description 13
- 238000000605 extraction Methods 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 55
- 238000011001 backwashing Methods 0.000 claims description 33
- 230000005540 biological transmission Effects 0.000 claims description 26
- 230000008676 import Effects 0.000 claims description 21
- 238000007789 sealing Methods 0.000 claims description 21
- 241000628997 Flos Species 0.000 claims description 19
- 238000005247 gettering Methods 0.000 claims description 14
- 238000004140 cleaning Methods 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 238000003825 pressing Methods 0.000 claims description 11
- 238000001914 filtration Methods 0.000 claims description 9
- 238000007790 scraping Methods 0.000 claims description 9
- 230000000694 effects Effects 0.000 claims description 8
- 238000005276 aerator Methods 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 3
- 238000002347 injection Methods 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 238000005265 energy consumption Methods 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 38
- 238000000926 separation method Methods 0.000 description 10
- 238000010586 diagram Methods 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 238000001035 drying Methods 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 210000002683 foot Anatomy 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 241000195493 Cryptophyta Species 0.000 description 3
- 239000002775 capsule Substances 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000002474 experimental method Methods 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
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model discloses a kind of liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put, including liquid impurity separating mechanism, liquid impurity concentration mechanism, liquid impurity dewatering device and liquid impurity mummification mechanism；Liquid impurity separating mechanism is filtered to mixing liquid to be separated impurity；Overlay on liquid impurity concentration mechanism to be arranged at below the first strainer of feed liquor canal bottom, liquid impurity concentrates mechanism and carries out preliminary hydro-extraction to the impurity filtered on the first strainer under retention and concentrated；Liquid impurity dewatering device is collected the first strainer and filters under retention and after concentration impurity, and press dewatering is carried out to which, liquid impurity dewatering device is connected with liquid impurity mummification mechanism, and liquid impurity mummification mechanism carries out mummification to the impurity after the dehydration of liquid impurity dewatering device and discharges the impurity after mummification.The device can be separated successively to impurities in liquid, concentrated, be dehydrated and mummification, and energy consumption is low, and floor space is little, wide with field.
Description
Technical field
This utility model is related to field of environment protection technical field, and more particularly to a kind of liquid impurity is separated, concentrates, taken off
Water and desiccation integral makeup are put.
Background technology
With the continuous development of social economy, human habitat suffers destroying increasingly.In environmental protection industry, usually can
Run into the problem for separating impurity in liquid.For example, black foul sewage water harnessing becomes nearest 2 years much-talked-about topics, in black foul sewage water harnessing
The important point is exactly solid-liquid separation, but existing solid-liquid separation technique efficiency is low, and floor space is big, black foul sewage water harnessing running cost
With higher.Additionally, the mankind discharge substantial amounts of nitrogen, phosphorus in water environment by production activity of living, occur river and lake tight
The body eutrophication of weight, algae amount reproduction therewith, causes river and lake anoxia, in turn results in river and lake ecological
Destruction, algae is efficiently separated from water body, is the key of river and lake ecosystem shift.However, to liquid in prior art
In body, the high efficiency separation of impurity, concentration, dehydration and mummification are generally relatively difficult, need the related efficient technology of urgent research and development.
Utility model content
The purpose of this utility model is to provide a kind of liquid impurity separation, concentration, dehydration and desiccation integral makeup and puts, to solve
The problem that certainly above-mentioned prior art is present, the device can separate to impurities in liquid successively, concentrate, be dehydrated and mummification,
Energy consumption is low, and floor space is little, wide with field.
For achieving the above object, this utility model provides following scheme：
This utility model provides a kind of liquid impurity separation, concentration, dehydration and desiccation integral makeup and puts, including liquid impurity
Separating mechanism, liquid impurity concentration mechanism, liquid impurity dewatering device and liquid impurity mummification mechanism；
The liquid impurity separating mechanism includes feed liquor canal, the first strainer and the first transmission wheel, and the feed liquor canal goes out liquid
End higher than liquid feeding end, the feed liquor canal include the front apron for being arranged on liquid feeding end and be arranged on the front apron both sides and with it is described
The side shield that front apron both sides are connected, is provided with water distributor on the front apron of the feed liquor canal, the feed liquor canal bottom is opened
Mouthful and the feed liquor canal bottom is covered with first strainer, first strainer is arranged in a ring；The first transmission wheel support exists
In first strainer, and drive first strainer to rotate, first strainer is moved along the canal bottom of the feed liquor canal；
The liquid impurity concentration mechanism is arranged at and overlays on below first strainer of the feed liquor canal bottom, the liquid
Body impurity concentrates mechanism and carries out preliminary hydro-extraction to the impurity filtered on first strainer under retention and concentrated；
The liquid impurity dewatering device is collected first strainer and filters under retention and after concentration impurity, and
Press dewatering is carried out to which, the liquid impurity dewatering device is connected with the liquid impurity mummification mechanism, and the liquid is miscellaneous
Matter mummification mechanism carries out mummification to the impurity after liquid impurity dewatering device dehydration and discharges the impurity after mummification.
Preferably, multiple apopores are evenly equipped with the water distributor；
The liquid impurity concentration mechanism includes negative tube and the first blower fan, and the negative tube is connected with first blower fan
Connect；
The negative tube is laid in the lower section of first strainer for overlaying on the feed liquor canal bottom, sets on the negative tube
It is equipped with the opening being in close contact with first strainer；
And/or, overlay on and below first strainer of the feed liquor canal bottom, there also is provided runner, the runner and institute
The tangent contact of the first strainer is stated, the runner can produce negative pressure in rotation or external force aspiration procedure.
Preferably, also including housing and strainer cleaning mechanism, the liquid impurity separating mechanism, liquid impurity concentration
Mechanism, the liquid impurity dewatering device, the liquid impurity mummification mechanism and the strainer cleaning mechanism are arranged at described
In housing, the lower housing portion is provided with support feet；The strainer cleaning mechanism includes scraping miscellaneous knife, gas backwashing system, air water
Backwashing system and gettering groove, it is described scrape miscellaneous cutter spacing in the first strainer side and with first strainer on the outside of offset；
The gas backwashing system and the air-water backwashing system are respectively positioned on the inner side of first strainer, and are respectively used to described
First strainer is along towards the direction gas injection and gas liquid mixture outside first strainer；It is provided with the gettering groove and institute
The opening of the first strainer close contact is stated, the gettering groove is connected with one second blower fan；The shower nozzle bag of the gas backwashing system
Include first gas import and gas outlet, the shower nozzle of the air-water backwashing system include second gas import, liquid-inlet and
Gas-liquid mixed is exported.
Preferably, the liquid impurity dewatering device includes waste-collecting box and spiral pressing dehydrator, and the waste-collecting box is located at
The first strainer side is simultaneously located at the lower section for scraping miscellaneous knife, and the spiral pressing dehydrator is located inside the waste-collecting box,
Described to scrape that miscellaneous knife is adjacent with the gas backwashing system, the effect for scraping miscellaneous knife by the gas backwashing system will be described
First strainer filters the impurity under retention and enters the waste-collecting box, and it is de- that squeezing is carried out to impurity by the spiral pressing dehydrator
Water, the bottom of the waste-collecting box are provided with first discharge port.
Preferably, the liquid impurity mummification mechanism includes mummification case, deflector and at least one mummification portion, the mummification
Box top is provided with impurity import, and the impurity import is connected with the first discharge port, and the mummification bottom portion is provided with
Two floss holes；The deflector is arranged in the mummification case and the gas flow pattern in mummification case is optimized, each described dry
Change portion is successively set in the deflector from top to bottom, and each mummification portion includes temperature controller, warming-up device, air blast
Machine, the second transmission wheel and the second strainer, second strainer are arranged in a ring, and second transmission wheel is supportted in second strainer
It is interior, and drive second strainer to rotate, the warming-up device is arranged on the lower section of second strainer, and the aerator is arranged
In the lower section of the warming-up device, the temperature controller controls the heating-up temperature of the warming-up device and heat time heating time.
Preferably, the input of second strainer is located at the lower section of the impurity import, two for being disposed adjacent mummification
In portion, lower section arrange the mummification portion second strainer input setting above the mummification portion it is described
The lower section of the outfan of the second strainer.
Preferably, sealing is provided between the feed liquor canal and first strainer, the sealing includes can regulating QI
The bottom of capsule and the sealing strip being arranged on adjustable air-bag, the bottom of the adjustable air-bag and the sealing strip is with described first
Strainer is in close contact.
Preferably, also including strainer tensioner and filter belt deviation corrector, the strainer tensioner is for by described
First strainer described in the outside stretching in inner side of one strainer；The filter belt deviation corrector is used to adjust first strainer described the
Position in one transmission wheel.
Preferably, also including catch box and circulating box；The catch box is arranged in first strainer and is located at described
Below feed liquor canal, for containing the liquid after the first strainer filtration described in, the catch box bottom is provided with the 3rd floss hole；Institute
Circulating box is stated below first strainer, for collecting the impurity that the air-water backwashing system flush falls, and by institute
The liquid of the clearance leakage between the canal bottom of the first strainer and the feed liquor canal is stated, the circulating box bottom is provided with the 4th discharge
Mouthful, the 4th floss hole is connected with the water inlet of the water distributor.
Preferably, the angle between the canal bottom of the feed liquor canal and horizontal plane is 0～30 °；First blower fan and described
Second blower fan is roots blower, and the outlet of the gettering groove is connected with the waste-collecting box；First transmission wheel includes one
First drivewheel and multiple first driven pulleys, second transmission wheel include second drivewheel and multiple second driven pulleys.
This utility model achieves following technique effect relative to prior art：
The liquid impurity that this utility model is provided is separated, is concentrated, dehydration and desiccation integral makeup are put, including liquid impurity point
Disembark structure, liquid impurity concentration mechanism, liquid impurity dewatering device and liquid impurity mummification mechanism；Liquid with impurity is led to
Cross water distributor and be passed through feed liquor canal, feed liquor canal bottom opening and be covered with the first strainer of annular setting, the first transmission wheel drive first
Strainer is rotated, and the first strainer is moved along the canal bottom of feed liquor canal, and the first strainer overlays on the part at canal bottom to the liquid in feed liquor canal
Filtered, liquid is separated with impurity, impurity is trapped within the first strainer；Liquid impurity concentrates mechanism and filters to first
Taking the impurity filtered under retention carries out preliminary hydro-extraction and is concentrated；Liquid impurity dewatering device is collected the filtration of the first strainer and is cut
Impurity stay and after concentration simultaneously carries out press dewatering to which, and the impurity after press dewatering is input into liquid impurity mummification
Mechanism, liquid impurity mummification mechanism carry out drying and other treatment to the impurity after the dehydration of liquid impurity dewatering device, and by mummification
Impurity afterwards is discharged, and realizes and impurities in liquid is separated successively, concentrate, be dehydrated and drying and other treatment, and the plant energy consumption is low,
Floor space is little, wide with field.
Description of the drawings
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment
Needed for accompanying drawing to be used be briefly described, it should be apparent that, drawings in the following description are only of the present utility model
Some embodiments, for those of ordinary skill in the art, without having to pay creative labor, can be with basis
These accompanying drawings obtain other accompanying drawings.
Fig. 1 is the structure of collection liquid impurity separation, concentration, dehydration and mummification multifunctional integrated device in this utility model
Schematic diagram；
Fig. 2 is the assembling schematic diagram of sealing in this utility model；
Fig. 3 is the assembling schematic diagram of gas backpurge system shower nozzle in this utility model；
Fig. 4 is the assembling schematic diagram of air water back washing system shower nozzle in this utility model；
Fig. 5 is the assembling schematic diagram of impurity anhydration system in this utility model；
Fig. 6 is the assembling schematic diagram of feed liquor canal and sealing in this utility model；
Fig. 7 be this utility model in collect liquid impurity separate, concentration, dehydration and mummification multifunctional integrated device it is another
Plant structural representation；
In figure：1- housings, 2- feed liquor canals, 201- front aprons, 202- side shields, 3- water distributors, 4- sealings, 5- first from
Driving wheel, 6- runners, 7- negative tubes, the first drivewheels of 8-, the first strainers of 9-, 10- strainer clamping systems, the 3rd floss holes of 11-,
12- catch boxs, 13- gas backpurge systems, 14- scrape miscellaneous knife, 15- air water back washing systems, 16- strainer deviation-rectifying systems, 17- gettering grooves,
18- support feets, 19- waste-collecting box, 20- spiral pressing dehydrators, 21- first discharge port, 22- circulating boxes, the 4th floss holes of 23-,
The second floss holes of 24-, 25- mummification casees, 26- adjustable air-bags, 27- sealing strips, 28- first gas imports, 29- gas outlets, 30-
Second gas import, the outlet of 31- gas-liquid mixeds, 32 impurity imports, 33- temperature controllers, the first driven pulleys of 34-, 35- heatings set
Standby, the first drivewheels of 36-, 37- aerators, the second strainers of 38-, 39- deflectors, 40- liquid-inlets.
Specific embodiment
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only this utility model a part of embodiment, rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment for being obtained, belongs to the scope of this utility model protection.
The purpose of this utility model is to provide a kind of liquid impurity separation, concentration, dehydration and desiccation integral makeup and puts, to solve
The problem that certainly above-mentioned prior art is present, the device can separate to impurities in liquid successively, concentrate, be dehydrated and mummification
Deng energy consumption is low, and floor space is little, wide with field.
It is understandable to enable above-mentioned purpose of the present utility model, feature and advantage to become apparent from, below in conjunction with the accompanying drawings and tool
Body embodiment is described in further detail to this utility model.
Embodiment one
The present embodiment provides a kind of liquid impurity separation, concentration, dehydration and desiccation integral makeup and puts, as shown in figure 1, including
Liquid impurity separating mechanism, liquid impurity concentration mechanism, liquid impurity dewatering device and liquid impurity mummification mechanism；
Liquid impurity separating mechanism includes feed liquor canal 2, the first strainer 9 and the first transmission wheel, as shown in fig. 6, feed liquor canal 2 is wrapped
The side shield 202 for including front apron 21 and being arranged on 201 both sides of front apron and be connected with 201 both sides of front apron, the front of feed liquor canal 2
Water distributor 3 is provided with plate 201, the rear end at 2 canal bottom of feed liquor canal is higher than liquid feeding end higher than front end, the i.e. liquid outlet of feed liquor canal, is entered
The horizontal tilt angle of liquid canal 2 is 0～30 °, beneficial to treating that remove impurity liquid is evenly distributed in the first strainer 9 with 2 canal bottom phase of feed liquor canal
On corresponding part, so as to be sufficiently carried out filtering.2 bottom opening of feed liquor canal and 2 bottom of feed liquor canal is covered with the first strainer 9, i.e.,
The front apron 201 and side shield 202 of feed liquor canal 2 is contacted with the first strainer 9, and the first strainer 9 is arranged in a ring；First transmission wheel
Support is in the first strainer 9, and drives the first strainer 9 to rotate, and the first strainer 9 is moved along the canal bottom of feed liquor canal 2；" interior " finger ring shape
In the ring of the first strainer 9, corresponding " outward " is represented outside the ring of the first strainer 9.In liquid impurity separating mechanism, the first strainer 9 exists
Constantly rotate in the presence of first transmission wheel so that the first strainer 9 carries out filterer to liquid with 2 corresponding part of feed liquor canal
Make, and walk to carry out the process of next step by the impurity band under retention is filtered.
Liquid impurity concentration mechanism is arranged at below first strainer 9 at 2 rear portion of feed liquor canal, and liquid impurity concentrates mechanism to the
The impurity filtered on one strainer 9 under retention carries out preliminary hydro-extraction, reduces the moisture of impurity and is concentrated；
Liquid impurity dewatering device is collected the first strainer 9 and filters under retention and after concentration impurity, and which is entered
Row press dewatering, liquid impurity dewatering device are connected with liquid impurity mummification mechanism, and liquid impurity mummification mechanism is to through liquid
Impurity after the dehydration of body impurity dewatering device carries out mummification and discharges the impurity after mummification.
The liquid impurity that the present embodiment is provided is separated, is concentrated, dehydration and desiccation integral makeup are put, during use, will be with miscellaneous
The liquid of matter is passed through feed liquor canal 2 by the inlet of water distributor 3,2 bottom opening of feed liquor canal and is covered with the first filter of annular setting
Band 9, first the first strainer of transmission wheel drive 9 are rotated, and the first strainer 9 is moved along the canal bottom of feed liquor canal 2, then the first strainer 9 covers
The liquid in feed liquor canal 2 is filtered in the part at 2 canal bottom of feed liquor canal, liquid is separated with impurity, impurity is trapped
On the first strainer 9；Liquid impurity concentrate mechanism preliminary hydro-extraction carried out to the impurity filtered on the first strainer 9 under retention and by its
Concentration；Liquid impurity dewatering device is collected the first strainer 9 and filters under retention and after concentration impurity and which is pressed
Dehydration is squeezed, the impurity after press dewatering is input into liquid impurity mummification mechanism, and liquid impurity mummification mechanism is to through liquid impurity
Impurity after dewatering device dehydration carries out drying and other treatment, and the impurity after mummification is discharged, and realizes to impurities in liquid successively
Separated, concentrate, be dehydrated and drying and other treatment, the plant energy consumption is low, and floor space is little, it is wide with field, can apply to dirt
Water factory's Central Plains sewage solid is separated, biological tank mud-water separation in Sewage Plant, and family's sewer feces are separated, the algae such as rivers and lakes
Separate, food processing factory's waste water solid is separated, slag separation etc. in mining wastewater
Embodiment two
The present embodiment is which includes the full content of embodiment one to one further improved embodiment of embodiment, i.e., originally
Embodiment provide liquid impurity separate, concentration, dehydration and desiccation integral makeup put comprising one liquid impurity of embodiment separate, it is dense
The entire infrastructure feature that contracting, dehydration and desiccation integral makeup are put, thes improvement is that：
Multiple apopores are evenly equipped with water distributor 3, mixed liquor can be evenly distributed on the first strainer 9, improved and filter
Efficiency and filter effect, as shown in figure 1, the first transmission wheel includes first drivewheel 8 and multiple first driven pulleys 5, first
The tangential velocity scope of drivewheel 8 is 0.01m/s-2m/s.First drivewheel 8 is arranged at the liquid outlet of feed liquor canal 2, feed liquor canal
Angle between 2 canal bottom and horizontal plane is 0～30 °.
Mechanism is concentrated including multiple liquid impurities, liquid impurity concentration mechanism includes negative tube 7 and the first blower fan, negative tube
7 are connected with the first blower fan, and the first blower fan is roots blower, and as one kind preferred embodiment, negative tube 7 is uniformly laid in and covers
Below the first strainer 9 of 2 bottom of feed liquor canal, the opening being in close contact with the first strainer 9, negative tube 7 on negative tube 7, are provided with
There is provided by roots blower and inside power, produce negative pressure, adsorb the moisture in the impurity on the first strainer, to the impurity after filtration
Carry out preliminary hydro-extraction and concentrate which.
As another preferred embodiment, as shown in figure 1, under 9 front portion of the first strainer covered of 2 bottom of feed liquor canal
Side, the i.e. part of A areas strainer 9, are disposed with multiple runners 6；The 9 tangent contact of runner 6 and the first strainer, runner 6 can be quick
In rotation process, external force suction is formed to the first strainer 9, negative pressure is produced, adsorbs the moisture in the impurity on the first strainer 9；It is negative
Pressure pipe 7 is laid in the lower section at 9 rear portion of the first strainer for overlaying on 2 bottom of feed liquor canal, the i.e. part of the first strainer of B1 areas 9.
As another preferred embodiment, as shown in fig. 7, the lower section cloth of the first strainer 9 covered by 2 bottom of feed liquor canal
It is provided with multiple runners 6 and multiple negative tubes 7,7 interval setting of runner 6 and negative tube, spaced runner 6 and negative tube 7
Quantity is not less than 1.
Using when, runner 6 rotate and stir the gas below the first strainer 9 formed negative pressure, be easy to treat that remove impurity liquid is a large amount of
And the first strainer 9 is quickly move through, the amount of filter liquid had both been improved, filter efficiency had been improved again.Runner 6 is to be capable of active rotation
Wheel, to rotate in application process high speed, the rotation direction of runner 6 may be configured as it is identical with the rotation direction of the first transmission wheel,
The rotation direction with the first transmission wheel be may also be configured to conversely, the scope of 6 tangential velocity of corresponding runner is set to 0.8m/s-
8m/s.Runner 6 improves treating capacity of first strainer 9 to biogas residue liquid, and runner 6 can destroy biogas slurry in running, not only
Surface tension on strainer, can also produce negative pressure, promote inflow-rate of water turbine of the biogas residue liquid on the first strainer 9 so that liquid with
Impurity is efficiently separated, and improves the removal of impurity in liquid.
As the present embodiment one kind preferred embodiment, the liquid impurity that the present embodiment is provided is separated, concentration, de-
Water and desiccation integral makeup are put
Structure, liquid impurity dewatering device, liquid impurity mummification mechanism and the strainer cleaning mechanism are arranged in housing 1, depart from into
The part of liquid canal 2 is cleaned in the presence of strainer cleaning mechanism, realizes filtration and cleaning while carrying out, clear without the need for shutting down
The first strainer 9 is managed, is conducive to liquid remove impurity persistently to carry out, improve efficiency.1 bottom of housing is provided with support feet 18, support feet 18
Support housing 1 and the mechanism inside housing 1.
Strainer cleaning mechanism includes scraping miscellaneous knife 14, gas backwashing system 13, air-water backwashing system 15 and gettering groove 17, scrapes
Miscellaneous knife 14 is located at 9 side of the first strainer and is offseted with the outside of the first strainer 9；Gas backwashing system 13 and air-water backwashing system
15 inner sides for being respectively positioned on the first strainer 9, and be respectively used to the first strainer 9 along towards the direction gas injection outside the first strainer 9
And gas liquid mixture, so as to clear up to the first strainer 9.
As shown in figure 3, the shower nozzle of gas backwashing system 13 includes first gas import 28 and gas outlet 29, first gas
Fluid in import 28 and gas outlet 29 is gas phase；As shown in figure 4, the shower nozzle of air-water backwashing system 15 includes the second gas
Body import 30, liquid-inlet 40 and gas-liquid mixed export 31, into the fluid in second gas import 30 and liquid-inlet 40 point
Not Wei gas phase and water phase, and the fluid for flowing out gas-liquid mixed outlet 31 is gas and water mixed phase.Air-water backwashing system 15 is than single
The mode of pure gas and water recoil has the effect of efficient cleaning strainer, and reduces energy consumption and water during device use
Consumption.The opening being in close contact with the first strainer 9 is provided with gettering groove 17, gettering groove 17 is connected with one second blower fan, the second wind
Machine is roots blower.
Liquid impurity dewatering device includes waste-collecting box 19 and spiral pressing dehydrator 20, and waste-collecting box 19 is located at the first strainer 9
Side is simultaneously located at the lower section for scraping miscellaneous knife 14, and 19 open top of waste-collecting box, the outlet of gettering groove 17 are connected with waste-collecting box 19, gettering groove
Impurity on 17 the first strainers 9 for absorbing is entered in waste-collecting box 19 and carries out processed.It is miscellaneous that spiral pressing dehydrator 20 is located at collection
Inside case 19, scrape that miscellaneous knife 14 is adjacent with gas backwashing system 13, scrape the impurity that miscellaneous knife 14 is scraped on the first strainer 9, and by gas
First strainer 9 is filtered the impurity under retention and enters waste-collecting box 19, by spiral pressing dehydrator 20 by the effect of backwashing system 13
Press dewatering is carried out to impurity, the bottom of waste-collecting box 19 is provided with first discharge port 21.In B2 areas, i.e. waste-collecting box 19, impurity contains
Water rate is further reduced.
As shown in figure 5, liquid impurity mummification mechanism includes mummification case 25, deflector 25 and at least one mummification portion, depth
Impurity after dehydration is emitted into mummification case 25 by first discharge port 21, and two mummification portions, mummification are preferably arranged in the present embodiment
Impurity import 32 is provided with the top of case 25, impurity import 32 is connected with first discharge port 21,25 bottom of mummification case is provided with second
Floss hole 24；Deflector 39 is arranged in mummification case 25 and the gas flow pattern in mummification case 25 is optimized, each mummification portion by
Top to bottm is successively set in deflector 39, and each mummification portion includes temperature controller 33, warming-up device 35, aerator 37, second
Transmission wheel and the second strainer 38, the second strainer 38 are arranged in a ring, and the second transmission wheel is supportted in the second strainer 38, and drives second
Strainer 38 is rotated, and the second transmission wheel includes second drivewheel 36 and multiple second driven pulleys 34, and warming-up device 35 is arranged on
The lower section of the second strainer 38, aerator 37 are arranged on the lower section of warming-up device 35, the control warming-up device 35 of temperature controller 33
Heating-up temperature and heat time heating time.The input of the second strainer 38 be located at impurity import 32 lower section, two of neighbouring setting
In mummification portion, second strainer 38 in the mummification portion of the input setting above of second strainer 38 in the mummification portion that lower section is arranged
Outfan lower section.
When liquid impurity mummification mechanism works, impurity is fallen on the second strainer 38 from mummification case import 32, by second actively
Wheel 36 and the second drive 34 drive the second strainer rotate, impurity in the transmitting procedure of the second strainer 38, in warming-up device 35
In the presence of aerator 37, its moisture content declines rapidly, and mummification the temperature inside the box controls warming-up device 35 by temperature control device 33 and obtains
Must stablize, gas flow pattern is optimized by deflector 39 in mummification case, be favorably improved the drying efficiency of biogas residue, the impurity of mummification
Discharged from the second floss hole 24.
As the present embodiment one kind preferred embodiment, the present embodiment provide liquid impurity separate, concentration, dehydration
And desiccation integral makeup is put, as shown in Fig. 2 sealing 4 is provided between feed liquor canal 2 and the first strainer 9, sealing 4 includes can
Regulating QI capsule 26 and the sealing strip 27 being arranged on adjustable air-bag, the bottom of adjustable air-bag 26 and the bottom of sealing strip 27 are with first
Strainer 9 is in close contact, and adjustable air-bag 26 and sealing strip 27 ensure that the seal between feed liquor canal 2 and the first strainer 9, by adjusting
26 air pressure inside of solar term capsule can adjust air bag 26 size of itself, indirectly such that it is able to adjust air bag 26 and the first strainer 9
Tactile tightness degree, it is ensured that feed liquor canal is watertight while also reduce the frictional force between more than 4 first strainer 9 of sealing as far as possible,
4 material of sealing is preferably rubber.
As the present embodiment one kind preferred embodiment, the present embodiment provide liquid impurity separate, concentration, dehydration
And desiccation integral makeup is put, as shown in figure 1, also including strainer tensioner 10 and filter belt deviation corrector 16, strainer tensioner
10, for outside the first strainer of stretching 9 in inner side by the first strainer, adjust the degree that runner 5 pushes against the first strainer 9, make the first filter
Band 9 tensioning or lax.Filter belt deviation corrector 16 is used to adjust position of first strainer 9 in the first transmission wheel, it is ensured that the first filter
With the 9 canal bottoms that can accurately and reliably overlay on feed liquor canal 2.
As the present embodiment one kind preferred embodiment, the present embodiment provide liquid impurity separate, concentration, dehydration
And desiccation integral makeup is put, as shown in figure 1, also including catch box 12 and circulating box 22；Catch box 12 is arranged in the first strainer 9
And be located at below feed liquor canal 2, for containing the liquid Jing after the first strainer 9 is filtered, 12 bottom of catch box is provided with the 3rd floss hole
11, liquid of the mixed liquor Jing after the filtration of the first strainer 9 is discharged by the 3rd floss hole 11 after entering catch box 12；Circulating box 22 is located at
Below first strainer 9,22 bottom of circulating box is provided with the 4th floss hole 23, and the 4th floss hole 23 is connected with the water inlet of water distributor 3,
Circulating box 22 collects impurity and the liquid that air-water backwashing system 15 is rinsed out, and by the first strainer 9 and the canal bottom of feed liquor canal 2
Between clearance leakage liquid, being passed through water distributor 3 by the 4th floss hole 23 carries out further filtration treatment.
Below with specific experiment introduction：
Process mixed liquor is Shandong Qu Feng food processing factories fermentation biogas residue liquid, according to following step, using different holes
The monolayer filter cloth in footpath is carried out separating, concentrates, is dehydrated and mummification test to biogas residue in water inlet.
Step one：Biogas residue liquid is passed through in feed liquor canal 2 by water distributor 3, biogas residue liquid is evenly distributed on the first strainer 9,
First strainer 9 is ring-type, and which is monolayer net, and aperture is 60um, is filtered by 2 the first strainer of lower end 9 of feed liquor canal, the first filter
Band 9 is driven by the first drivewheel 8 and is driven with the first driven pulley 5, and 11 tangential velocity of the first drivewheel is 0.8m/s, the first strainer 9
Horizontal tilt angle is α, and strainer inclined angle alpha is 13 degree, prevents mixed liquor big in feed liquor canal 2 and 9 contact surface of strainer using sealing 4
Amount leakage, the first strainer 9 are operationally in close contact with the D and E part of sealing 4, on the downside of the part of the first strainer of A areas 9
Some runners 6 are arranged, treating capacity of the strainer 9 to biogas residue liquid is improved, runner 6 in running, not only can destroy biogas slurry and exist
Surface tension on strainer, can also produce negative pressure, promote inflow-rate of water turbine of the biogas residue liquid on the first strainer 9, the tangent line speed of runner 6
Spend for 0.8m/s；
Step 2：The part of first strainer 9 of the biogas residue in biogas residue liquid below 3 front end of water distributor, namely in A areas strainer
9 part, is efficiently separated and is concentrated, and the biogas residue clearance wherein in biogas slurry is 65%, and biogas residue concentration improves 2.5
Times, the biogas residue after concentration has obtained preliminary dehydration using the negative tube 7 for being arranged on B1 areas, and impurity moisture content is 93%；Biogas residue
The isolated biogas slurry of liquid is discharged by first discharge port 11 after entering catch box 12, using scraping miscellaneous knife 14 and by gas backwash system
The effect of system 16, the biogas residue of preliminary hydro-extraction is entered and be further dehydrated biogas residue by spiral pressing dehydrator 20 after waste-collecting box 19,
Biogas residue moisture content in the waste-collecting box 19 in B2 areas is further decreased to 88%, and the biogas residue after deep dehydration is by first discharge port 21
Discharge, ensures the stable operation of the first strainer 9 of rotation using strainer tensioner 10 and filter belt deviation corrector 16；
Step 3：Biogas residue after deep dehydration is drained into mummification case 25 by first discharge port 21, after biogas residue mummification, by second
Floss hole 24 is discharged, and moisture content of the biogas residue after the process of C areas is reduced to 20%；
Second strainer 38 is ring-type single or multiple lift strainer, and aperture is 100um.
Step 4：The first strainer 9 after being polluted by biogas residue liquid utilizes gas backwashing system 16 and air-water backwashing system 15
High-efficiency cleaning is obtained, during the process of whole mixed liquor, the biogas residue liquid of leakage and is rinsed by air-water backwashing system 15
The biogas residue fallen is discharged by the 4th floss hole 23 after being collected by circulating box 22, and being passed through water distributor 3 carries out further filtration treatment.
Apply specific case to be set forth principle of the present utility model and embodiment in this utility model, the above
The explanation of embodiment is only intended to help and understands method of the present utility model and its core concept；Simultaneously for the one of this area
As technical staff, according to thought of the present utility model, will change in specific embodiments and applications.To sum up
Described, this specification content is should not be construed as to restriction of the present utility model.
Claims (10)
1. a kind of liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Separate including liquid impurity
Mechanism, liquid impurity concentration mechanism, liquid impurity dewatering device and liquid impurity mummification mechanism；
The liquid impurity separating mechanism includes feed liquor canal, the first strainer and the first transmission wheel, and the liquid outlet of the feed liquor canal is high
In liquid feeding end, the feed liquor canal include the front apron for being arranged on liquid feeding end and be arranged on the front apron both sides and with the front
The side shield that plate both sides are connected, is provided with water distributor on the front apron of the feed liquor canal, the feed liquor canal bottom opening and
The feed liquor canal bottom is covered with first strainer, and first strainer is arranged in a ring；First transmission wheel is supportted described
In first strainer, and drive first strainer to rotate, first strainer is moved along the canal bottom of the feed liquor canal；
The liquid impurity concentration mechanism is arranged at and overlays on below first strainer of the feed liquor canal bottom, and the liquid is miscellaneous
Matter concentrates mechanism and carries out preliminary hydro-extraction to the impurity filtered on first strainer under retention and concentrated；
The liquid impurity dewatering device is collected first strainer and filters under retention and after concentration impurity, and to which
Press dewatering is carried out, the liquid impurity dewatering device is connected with the liquid impurity mummification mechanism, the liquid impurity is done
Changing mechanism carries out mummification to the impurity after liquid impurity dewatering device dehydration and discharges the impurity after mummification.
2. liquid impurity according to claim 1 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：
Multiple apopores are evenly equipped with the water distributor；
The liquid impurity concentration mechanism includes negative tube and the first blower fan, and the negative tube is connected with first blower fan；
The negative tube is laid in the lower section of first strainer for overlaying on the feed liquor canal bottom, is provided with the negative tube
The opening being in close contact with first strainer；
And/or, overlay on and below first strainer of the feed liquor canal bottom, there also is provided runner, the runner and described
The tangent contact of one strainer, the runner can produce negative pressure in rotation or external force aspiration procedure.
3. liquid impurity according to claim 2 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Also
Including housing and strainer cleaning mechanism, the liquid impurity separating mechanism, liquid impurity concentration mechanism, the liquid impurity
Dewatering device, the liquid impurity mummification mechanism and the strainer cleaning mechanism are arranged in the housing, under the housing
Portion is provided with support feet；The strainer cleaning mechanism includes scraping miscellaneous knife, gas backwashing system, air-water backwashing system and gettering
Groove, it is described scrape miscellaneous cutter spacing in the first strainer side and with first strainer on the outside of offset；The gas backwashing system
The inner side of first strainer is respectively positioned on the air-water backwashing system, and is respectively used to first strainer along towards institute
State direction gas injection and the gas liquid mixture outside the first strainer；It is provided with the gettering groove and closely connects with first strainer
Tactile opening, the gettering groove are connected with one second blower fan；The shower nozzle of the gas backwashing system include first gas import and
Gas outlet, the shower nozzle of the air-water backwashing system include second gas import, liquid-inlet and gas-liquid mixed export.
4. liquid impurity according to claim 3 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Institute
Stating liquid impurity dewatering device includes waste-collecting box and spiral pressing dehydrator, and the waste-collecting box is located at the first strainer side simultaneously
Positioned at the lower section for scraping miscellaneous knife, the spiral pressing dehydrator is located inside the waste-collecting box, described to scrape miscellaneous knife with the gas
Backwashing system is adjacent, the effect for scraping miscellaneous knife by the gas backwashing system, and first strainer is filtered under retention
Impurity enter the waste-collecting box, and press dewatering, the bottom of the waste-collecting box are carried out to impurity by the spiral pressing dehydrator
Portion is provided with first discharge port.
5. liquid impurity according to claim 4 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Institute
Stating liquid impurity mummification mechanism includes mummification case, deflector and at least one mummification portion, and the mummification box top is provided with impurity
Import, the impurity import are connected with the first discharge port, and the mummification bottom portion is provided with the second floss hole；The water conservancy diversion
Plate is arranged in the mummification case and the gas flow pattern in mummification case is optimized, and each mummification portion is set from top to bottom successively
Put in the deflector, each mummification portion includes temperature controller, warming-up device, aerator, the second transmission wheel and second
Strainer, second strainer are arranged in a ring, and second transmission wheel is supportted in second strainer, and drive second filter
Band is rotated, and the warming-up device is arranged on the lower section of second strainer, and the aerator is arranged under the warming-up device
Side, the temperature controller control the heating-up temperature of the warming-up device and heat time heating time.
6. liquid impurity according to claim 5 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Institute
The input for stating the second strainer is located at the lower section of the impurity import, in two for being disposed adjacent mummification portion, the institute that lower section is arranged
State the outfan of second strainer in the mummification portion of the input setting above of second strainer in mummification portion
Lower section.
7. liquid impurity according to claim 6 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Institute
State and between feed liquor canal and first strainer, be provided with sealing, the sealing includes adjustable air-bag and is arranged on adjustable air-bag
On sealing strip, the bottom of the bottom of the adjustable air-bag and the sealing strip is in close contact with first strainer.
8. liquid impurity according to claim 7 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Also
Including strainer tensioner and filter belt deviation corrector, the strainer tensioner is for outwards being supportted by the inner side of first strainer
Tight first strainer；The filter belt deviation corrector is used to adjust position of first strainer in first transmission wheel.
9. liquid impurity according to claim 8 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：Also
Including catch box and circulating box；The catch box is arranged in first strainer and is located at below the feed liquor canal, for containing
Liquid after dress the first strainer filtration described in, the catch box bottom is provided with the 3rd floss hole；The circulating box is located at described
Below first strainer, for collecting the impurity that the air-water backwashing system flush falls, and by first strainer with it is described
The liquid of the clearance leakage between the canal bottom of feed liquor canal, the circulating box bottom are provided with the 4th floss hole, the 4th floss hole
Connect with the water inlet of the water distributor.
10. liquid impurity according to claim 9 is separated, is concentrated, dehydration and desiccation integral makeup are put, it is characterised in that：
Angle between the canal bottom of the feed liquor canal and horizontal plane is 0～30 °；First blower fan and second blower fan are Roots
Blower fan, the outlet of the gettering groove are connected with the waste-collecting box；First transmission wheel includes first drivewheel and multiple
First driven pulley, second transmission wheel include second drivewheel and multiple second driven pulleys.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621082211.5U CN206045549U (en) | 2016-09-26 | 2016-09-26 | Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621082211.5U CN206045549U (en) | 2016-09-26 | 2016-09-26 | Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206045549U true CN206045549U (en) | 2017-03-29 |
Family
ID=58366694
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621082211.5U Active CN206045549U (en) | 2016-09-26 | 2016-09-26 | Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206045549U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237692A (en) * | 2016-09-26 | 2016-12-21 | 尚川（北京）水务有限公司 | Liquid impurity separates, concentrates, is dehydrated and desiccation integral gasifying device |
| CN112657823A (en) * | 2019-10-15 | 2021-04-16 | 湖南省益能环保科技有限公司 | Electric material distributing device for dried sludge |
| CN113750615A (en) * | 2021-08-26 | 2021-12-07 | 中煤（北京）环保工程有限公司 | Vacuum drying type filter press tool and filter pressing method thereof |
| CN114225521A (en) * | 2021-12-29 | 2022-03-25 | 威海丰泰新材料科技股份有限公司 | Filter belt type superfine grating machine |
-
2016
- 2016-09-26 CN CN201621082211.5U patent/CN206045549U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106237692A (en) * | 2016-09-26 | 2016-12-21 | 尚川（北京）水务有限公司 | Liquid impurity separates, concentrates, is dehydrated and desiccation integral gasifying device |
| CN112657823A (en) * | 2019-10-15 | 2021-04-16 | 湖南省益能环保科技有限公司 | Electric material distributing device for dried sludge |
| CN113750615A (en) * | 2021-08-26 | 2021-12-07 | 中煤（北京）环保工程有限公司 | Vacuum drying type filter press tool and filter pressing method thereof |
| CN113750615B (en) * | 2021-08-26 | 2022-09-16 | 中煤（北京）环保工程有限公司 | Vacuum drying type filter press tool and filter pressing method thereof |
| CN114225521A (en) * | 2021-12-29 | 2022-03-25 | 威海丰泰新材料科技股份有限公司 | Filter belt type superfine grating machine |
| CN114225521B (en) * | 2021-12-29 | 2023-03-14 | 威海丰泰新材料科技股份有限公司 | Filter belt type superfine grating machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN206045549U (en) | Liquid impurity is separated, is concentrated, dehydration and desiccation integral makeup are put | |
| CN106237692B (en) | Liquid impurity separation, concentration, dehydration and desiccation integral makeup are put | |
| CN106365370A (en) | Recycled type sewage purification equipment | |
| CN207175619U (en) | A kind of Water purification filter | |
| CN113041691A (en) | Sludge press filtration water-saving flushing device | |
| CN105251254A (en) | Variable type bidirectional flow high-speed fiber filter | |
| CN209449489U (en) | A kind of environment-friendly type industrial circulating water cultivating system | |
| CN110922027A (en) | Sludge dewatering, deodorizing and drying device with solar panel heating | |
| CN206720774U (en) | A kind of blow-off pipe with sewage water filtration function | |
| CN206720958U (en) | The system that high efficient solid and liquid separation secondary filter handles black and odorous water | |
| CN107445269A (en) | A kind of water quality ensuring equipment based on Mechanical Driven pulse clarifying equipment | |
| CN210645450U (en) | Kitchen garbage centrifugal filtration takes off liquid device in coordination | |
| CN209010275U (en) | A kind of feather processing sewage-treatment plant | |
| CN203668143U (en) | Liquid-solid separation device for quenched water and washing water in MTO (methanol to olefins) | |
| CN208649012U (en) | A kind of small-scale sewage processing sewage water filtration recyclable device of cleaning easy to disassemble | |
| CN208898701U (en) | Glass reinforced plastic biochemistry pool | |
| CN215924600U (en) | Prevent blockking up sewage treatment plant convenient to purify domestic waste water | |
| CN207957954U (en) | A kind of ore cleaning sullage filtration processing equipment of environmental protection | |
| CN210620524U (en) | Utilize new forms of energy rivers to filter hierarchical utilization device | |
| CN206285570U (en) | A kind of river course multiphase microfiltration equipment | |
| CN216711864U (en) | Sludge treatment circulation washing unit | |
| CN208641878U (en) | A kind of concentrator | |
| CN204185343U (en) | A kind of waste disposal plant | |
| CN216737893U (en) | Purifying sewage treatment filtering and recycling device | |
| CN221332910U (en) | Sewage treatment discharging equipment for water purification plant |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20231007 Address after: 101399 north of wenyuying village, Gaoliying Town, Shunyi District, Beijing Patentee after: SHINE (BEIJING) WATER CO.,LTD. Patentee after: Shangchuan (Beijing) Equipment Co.,Ltd. Address before: Room 3009, 3rd Floor, Municipal Office Building, No. 2, Guangximen Road, Haidian District, Beijing, 100089 Patentee before: SHINE (BEIJING) WATER CO.,LTD. |