CN106365238A - Powdered activated carbon dry-method feeding system - Google Patents
Powdered activated carbon dry-method feeding system Download PDFInfo
- Publication number
- CN106365238A CN106365238A CN201610780839.0A CN201610780839A CN106365238A CN 106365238 A CN106365238 A CN 106365238A CN 201610780839 A CN201610780839 A CN 201610780839A CN 106365238 A CN106365238 A CN 106365238A
- Authority
- CN
- China
- Prior art keywords
- discharging
- activated carbon
- powdered activated
- control valve
- discharge
- 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.)
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- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 238000000034 method Methods 0.000 title claims abstract description 29
- 230000007246 mechanism Effects 0.000 claims abstract description 77
- 238000007599 discharging Methods 0.000 claims abstract description 66
- 239000003814 drug Substances 0.000 claims description 24
- 239000000463 material Substances 0.000 claims description 20
- 229940079593 drug Drugs 0.000 claims description 12
- 241000220324 Pyrus Species 0.000 claims description 4
- 235000021017 pears Nutrition 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 238000011010 flushing procedure Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 239000012254 powdered material Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 11
- 230000006872 improvement Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 6
- 230000000903 blocking effect Effects 0.000 description 3
- 238000001514 detection method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 230000009471 action Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- JXTHNDFMNIQAHM-UHFFFAOYSA-N dichloroacetic acid Chemical compound OC(=O)C(Cl)Cl JXTHNDFMNIQAHM-UHFFFAOYSA-N 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- WEVYAHXRMPXWCK-UHFFFAOYSA-N methyl cyanide Natural products CC#N WEVYAHXRMPXWCK-UHFFFAOYSA-N 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- HSQFVBWFPBKHEB-UHFFFAOYSA-N 2,3,4-trichlorophenol Chemical compound OC1=CC=C(Cl)C(Cl)=C1Cl HSQFVBWFPBKHEB-UHFFFAOYSA-N 0.000 description 1
- ISPYQTSUDJAMAB-UHFFFAOYSA-N 2-chlorophenol Chemical compound OC1=CC=CC=C1Cl ISPYQTSUDJAMAB-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 229960005215 dichloroacetic acid Drugs 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 235000021050 feed intake Nutrition 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- YNJBWRMUSHSURL-UHFFFAOYSA-N trichloroacetic acid Chemical compound OC(=O)C(Cl)(Cl)Cl YNJBWRMUSHSURL-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Air Transport Of Granular Materials (AREA)
Abstract
The invention discloses a powdered activated carbon dry-method feeding system which comprises a feed charging station, wherein the feed charging station is connected with a feeding mechanism; the lower side of the feeding mechanism is connected with a feed bin; the upper part of the feed bin is provided with a roof scrubber, and the lower part of the feed bin is provided with a discharge valve; the lower end of the discharge valve is provided with a discharging mechanism; a discharging end of the discharging mechanism is connected with a blanking mechanism; the lower side of the blanking mechanism is provided with a jet mixer connected with a water supply pipe; the jet mixer is connected with a chemical discharging mechanism. The powdered activated carbon dry-method feeding system is stable and reliable in working performance and uniform in powdered material charging and blanking, is capable of avoiding flushing and blockage of pipelines, realizing automatic operation during the whole process, greatly improving the production efficiency, reducing manpower resources, realizing sealed operation in the whole process and avoiding environmental pollution.
Description
Technical field
The present invention relates to a kind of adding equipment, more particularly, to a kind of Powdered Activated Carbon dry method dosing system.
Background technology
The use history of existing 70 years about in Water purification for the Powdered Activated Carbon.Since the U.S. is lived using powder first
Property charcoal remove the odor that chlorophenol produces after, activated carbon become remove in Water purification color, smell, the effective ways of taste and Organic substance
One of.The external numerous studies that powder electroless plating performance is made show: Powdered Activated Carbon to trichlorophenol, 2,4,6,-T, chlorophenesic acid,
Contained Organic substance in pesticide, haloform and precursor and disinfection byproduct (DBP) trichloroacetic acid, dichloroacetic acid and dihalo- acetonitrile etc.
There is good adsorption effect Deng all, check colors, smell, the removal effect of taste gains public acceptance.
Powdered Activated Carbon is very universal in Europe, the United States, Deng state, and the U.S.'s initial stage eighties is used in Water purification every year
About 2.5 ten thousand tons of Powdered Activated Carbon, and have increase trend year by year.China start in the latter stage sixties to note polluted source except smelling, remove
Taste problem.Powdered Activated Carbon was all once tried out in Shanghai, Harbin, Hefei, Guangzhou, and in recent years, China is to Powdered Activated Carbon
Research and application are gradually paid attention to.
Powdered Activated Carbon adds technical field at present, there is problems with, the pollution problem of dust from flying in application, work
Bad environments, load and unload, unpack, preparing, add during high labor intensive, in application, accurate quantification adds and is difficult to control to, automatically
Change that controlling extent is low, due to failing to solve well limitation that this technology exists in application aspect it is difficult to performance powder activity
The advantage of charcoal technology.
Content of the invention
The present invention provides a kind of stable and reliable working performance, adds powder blanking uniform, it is to avoid the flushing of pipeline and blocking,
Can be operated with whole-course automation, improve production efficiency, reduce human resourcess, and whole " locked in " operation, it is to avoid cause environment dirty
The Powdered Activated Carbon dry method dosing system of dye.
For solving above-mentioned technical problem, the technical scheme is that a kind of Powdered Activated Carbon dry method dosing system, including
Feeding station, described feeding station is connected with feed mechanism, and the lower section of described feed mechanism is connected with feed bin, and the top of described feed bin sets
There is roof scrubber, the bottom of described feed bin is provided with discharge valve, and the lower end of described discharge valve is provided with discharging mechanism, described discharging machine
The discharge end of structure is connected with blanking mechanism, and the lower section of described blanking structure is provided with the jet mixer being connected with supply line, institute
State jet mixer and be connected with medicament discharge mechanism.
As preferred technical scheme, described feed mechanism includes vacuum feeder, and described vacuum feeder is provided with installation
In the feeder vacuum tank on the top of described feed bin, the low side of described feeder vacuum tank is connected with described feeding station, described on
The high-end of material machine vacuum tank is connected with feeding blower fan.
As preferred technical scheme, also include source of the gas feed mechanism, it is anti-that described source of the gas feed mechanism is connected with feeding station
Blow control valve, vacuum tank blowback control valve and cleaner unit blowback control valve, described feeding station blowback control valve, described vacuum tank are anti-
Blow control valve and described cleaner unit blowback control valve is connected respectively described feeding station, described feeder vacuum tank and described storehouse
Top cleaner unit；Source of the gas feed mechanism is connected with Arch-Breaking Device air source control valve, and described Arch-Breaking Device air source control valve is connected with and is arranged on
Bulkhead Arch-Breaking Device on described feed bin.
As the improvement to technique scheme, described discharging mechanism is included horizontally arranged and is connected with described discharge valve
The discharge nozzle connecing, one end of described discharge nozzle is provided with discharging machine, and described discharging machine drive connection has positioned at described discharge nozzle
Interior discharging axle, described discharging axle is provided with the discharge blade of spiral setting.
As the improvement to technique scheme, between described discharge valve and described discharge nozzle, it is provided with the loose mechanism of discharging,
The loose mechanism of described discharging includes the loose axle of horizontally arranged discharging, and the loose axle of described discharging is connected with the loose electricity of discharging
Machine, the loose axle of described discharging is provided with pears blade blade.
As the improvement to technique scheme, described blanking mechanism includes the blanking being connected with the discharge end of discharge nozzle
Pipe, described material blanking tube vertical direction setting, described material blanking tube is provided with blanking control valve, and the lower end connection of described material blanking tube is described
Jet mixer.
As the improvement further to technique scheme, described material blanking tube is also associated with the premix being connected with supply line
Pipe, described premix barrel is provided with premix control valve.
As the improvement further to technique scheme, described medicament discharge mechanism includes the drug being connected with jet mixer
Pipe, described drug discharging tube is provided with drug control valve.
As the improvement further to technique scheme, described blanking mechanism, described jet mixer and described drug
The quantity of mechanism is respectively two.
As the further improvement to technique scheme, described feed bin be respectively equipped with from the bottom to top lower level-sensing device, in
Level-sensing device and high charge level meter.
Due to employing technique scheme, a kind of Powdered Activated Carbon dry method dosing system, including feeding station, feeding station is even
It is connected to feed mechanism, the lower section of feed mechanism is connected with feed bin, and the top of feed bin is provided with roof scrubber, and the bottom of feed bin is provided with
Discharge valve, the lower end of discharge valve is provided with discharging mechanism, and the discharge end of discharging mechanism is connected with blanking mechanism, the lower section of blanking structure
It is provided with the jet mixer being connected with supply line, jet mixer is connected with medicament discharge mechanism.Packed Powdered Activated Carbon is passed through
Pour feeding station into after artificial unpacking, start feed mechanism and roof scrubber, in feeding station, powder is transported to feed bin.Add
When, open discharge valve, discharging mechanism and blanking mechanism, make blanking channel smooth, water is mixed with Powdered Activated Carbon by jet mixer
After conjunction, jet, to medicament discharge mechanism, is added to toss area.Stable and reliable working performance of the present invention, adds powder blanking uniform, it is to avoid
The flushing of pipeline and blocking, can be operated with whole-course automation, substantially increase production efficiency, decrease human resourcess, and
Whole " locked in " operation, it is to avoid cause environmental pollution.
Brief description
The following drawings is only intended to, in doing schematic illustration and explanation to the present invention, not delimit the scope of the invention.Wherein:
Fig. 1 is the structural representation of the embodiment of the present invention one；
Fig. 2 is the structure principle chart in a portion of the embodiment of the present invention one；
Fig. 3 is the structural representation of the embodiment of the present invention two.
In figure: 1- feeding station；21- feeder vacuum tank；22- feeding blower fan；3- feed bin；31- discharge valve；Material position under 32-
Meter；Level-sensing device in 33-；34- high charge level meter；35- roof scrubber；4- discharge nozzle；41- discharging machine；42- discharging loosening machine
Structure；5- blanking mechanism；51- material blanking tube；52- blanking control valve；53- premix barrel；54- premixes control valve；55- jet mixer；
61- source of the gas feed mechanism；62- feeding station blowback control valve；63- vacuum tank blowback control valve；64- cleaner unit blowback control valve；
65- Arch-Breaking Device air source control valve；66- bulkhead Arch-Breaking Device；7- drug discharging tube；71- drug control valve；8- supply line.
Specific embodiment
With reference to the accompanying drawings and examples, the present invention is expanded on further.In the following detailed description, only pass through explanation
Mode describes some one exemplary embodiment of the present invention.Undoubtedly, those of ordinary skill in the art will be consequently realised that,
In the case of without departing from the spirit and scope of the present invention, can by with various different in the way of described embodiment is repaiied
Just.Therefore, accompanying drawing and description are inherently illustrative, rather than are used for limiting scope of the claims.
Embodiment one: as depicted in figs. 1 and 2, a kind of Powdered Activated Carbon dry method dosing system, including feeding station 1, feeding station
1 is connected with feed mechanism, and the lower section of feed mechanism is connected with feed bin 3, and the top of feed bin 3 is provided with roof scrubber 35, feed bin 3
Bottom is provided with discharge valve 31, and the lower end of discharge valve 31 is provided with discharging mechanism, and the discharge end of discharging mechanism is connected with blanking mechanism 5,
The lower section of blanking structure is provided with the jet mixer 55 being connected with supply line 8, and jet mixer 55 is connected with medicament discharge mechanism.Will
Packed Powdered Activated Carbon pours feeding station 1 after artificial unpacking into, starts feed mechanism and roof scrubber 35, in feeding station 1
Powder is transported to feed bin 3.When adding, open discharge valve 31, discharging mechanism and blanking mechanism 5, make blanking channel smooth, jet
Blender 55 water is mixed with Powdered Activated Carbon after jet to medicament discharge mechanism, be added to toss area.
Feed mechanism includes vacuum feeder, and vacuum feeder is provided with the feeder vacuum tank on the top being arranged on feed bin 3
21, the low side of feeder vacuum tank 21 is connected with feeding station 1, and the high-end of feeder vacuum tank 21 is connected with feeding blower fan 22.If
Reserve vacuum feeder suction blanking time interval, open feeding blower fan 22, in feeder vacuum tank 21, produce negative pressure, feeding station
Powdered Activated Carbon in 1 is inhaled in feeder vacuum tank 21, when feeding blower fan 22 quits work, in feeder vacuum tank 21
Powdered Activated Carbon drop in feed bin 3, said structure is capable of automatic charging, closing conveying, prevents dust from flying, saves time
Laborsaving.
Also include source of the gas feed mechanism 61, it is anti-that source of the gas feed mechanism 61 is connected with feeding station blowback control valve 62, vacuum tank
Blow control valve 63 and cleaner unit blowback control valve 64, feeding station blowback control valve 62, vacuum tank blowback control valve 63 and cleaner unit
Blowback control valve 64 is connected respectively feeding station 1, feeder vacuum tank 21 and roof scrubber 35；Source of the gas feed mechanism 61 is even
It is connected to Arch-Breaking Device air source control valve 65, Arch-Breaking Device air source control valve 65 is connected with the bulkhead Arch-Breaking Device 66 being arranged on feed bin 3.
Source of the gas feed mechanism 61 provides gas, controls the keying of feeding station blowback control valve 62, is capable of to feeding station 1
Carry out blowback, it is to avoid Powdered Activated Carbon accumulated plugging in feeding station 1；Control the keying of vacuum tank blowback control valve 63, can
Realize carrying out blowback to feeder vacuum tank 21, it is to avoid Powdered Activated Carbon accumulated plugging in feeder vacuum tank 21；Control removes
The keying of dirt device blowback control valve 64, is capable of carrying out blowback to roof scrubber 35, it is to avoid Powdered Activated Carbon removes in silo roof
Accumulated plugging in dirt device 35；Control the keying of Arch-Breaking Device air source control valve 65, bulkhead Arch-Breaking Device 66 action can be made, it is to avoid powder
Activated carbon accumulated plugging in feed bin 3, and hole shakes, efficient broken arch, effectively prevents powder cavity, improves and feed intake accurately
Degree.
Source of the gas feed mechanism 61 can include air compressor, and air compressor connects air accumulator, and air accumulator connects free
Gas drying machine, finally transfers out pressure and the satisfactory source of the gas of humidity by dried-air drier.
Discharging mechanism includes discharge nozzle 4 that is horizontally arranged and being connected with discharge valve 31, and one end of discharge nozzle 4 is provided with out
Material motor 41, discharging machine 41 drive connection has the discharging axle in discharge nozzle 4, and discharging axle is provided with the discharging of spiral setting
Blade.Open discharge valve 31, the Powdered Activated Carbon in feed bin 3 drops in discharge nozzle 4, discharging machine 41 work drives discharging axle
And discharge blade, make Powdered Activated Carbon move to discharge nozzle 4 discharge end in discharge nozzle 4.Discharging machine 41 is frequency conversion motor, energy
Enough adjust discharging speed, control discharging speed.
It is provided with the loose mechanism of discharging 42, the loose mechanism of discharging 42 includes horizontal direction and sets between discharge valve 31 and discharge nozzle 4
The loose axle of discharging put, the loose axle of discharging is connected with the loose motor of discharging, and the loose axle of discharging is provided with pears blade blade.In discharging
During, the loose motor of discharging drives the loose axle of discharging and pears blade blade, Powdered Activated Carbon is stirred, can play
Fluffing action well, it is to avoid powder accumulated plugging.
Blanking mechanism 5 includes the material blanking tube 51 being connected with the discharge end of discharge nozzle 4, and material blanking tube 51 vertical direction is arranged, and falls
Expects pipe 51 is provided with blanking control valve 52, and the lower end of material blanking tube 51 connects jet mixer 55.Open blanking control valve 52, by going out
The Powdered Activated Carbon that expects pipe 4 transfers out drops into material blanking tube 51 it is ensured that Powdered Activated Carbon is transported to jet mixer 55.
Material blanking tube 51 is also associated with the premix barrel 53 being connected with supply line 8, and premix barrel 53 is provided with premix control valve 54,
Open premix control valve 54, can allow water to flow in premix barrel 53, Powdered Activated Carbon is premixed, be then transported to jet again and mix
Clutch 55.
Medicament discharge mechanism includes the drug discharging tube 7 being connected with jet mixer 55, and drug discharging tube 7 is provided with drug control valve 71, on
State structure can conveniently control.
Feed bin 3 is respectively equipped with lower level-sensing device 32, middle level-sensing device 33 and high charge level meter 34 from the bottom to top, lower level-sensing device 32, in
Level-sensing device 33 and high charge level meter 34 are connected with plc switch board, lower level-sensing device 32 detection signal, when Powdered Activated Carbon is located at lower material position
During meter less than 32, report to the police and stop discharging mechanism helical feed；Middle level-sensing device 33 detection signal, when Powdered Activated Carbon is located at middle material position
Below and during lower level-sensing device more than 32, remind feeding；High charge level meter 34 detection signal, when Powdered Activated Carbon is higher than high charge level meter 34
When, report to the police and limit feeding.
Certainly plc can also control each motor of connection and control valve, is capable of Automated condtrol, for the skill of this area
For art personnel, automated control technology is known technology, will not be described here.
The present embodiment stable and reliable working performance, adds powder blanking uniform, it is to avoid the flushing of pipeline and blocking, permissible
Whole-course automation operates, and substantially increases production efficiency, decreases human resourcess, and whole " locked in " operation, it is to avoid cause ring
Border is polluted.
Embodiment two: as shown in figure 3, embodiment two is with the difference of embodiment one, blanking mechanism 5, jet mix
The quantity of clutch 55 and medicament discharge mechanism is respectively two, two blanking mechanisms 5 can blanking simultaneously, and be respectively delivered to corresponding
Jet mixer 55, medicament discharge mechanism, realize discharging simultaneously, substantially increase work efficiency.
Ultimate principle, principal character and the advantages of the present invention of the present invention have been shown and described above.The technology of the industry
, it should be appreciated that the present invention is not restricted to the described embodiments, the simply explanation described in above-described embodiment and description is originally for personnel
The principle of invention, without departing from the spirit and scope of the present invention, the present invention also has various changes and modifications, these changes
Change and improvement both falls within scope of the claimed invention.Claimed scope by appending claims and its
Equivalent thereof.
Claims (10)
1. a kind of Powdered Activated Carbon dry method dosing system, including feeding station it is characterised in that: described feeding station is connected with feeder
Structure, the lower section of described feed mechanism is connected with feed bin, and the top of described feed bin is provided with roof scrubber, and the bottom of described feed bin sets
There is discharge valve, the lower end of described discharge valve is provided with discharging mechanism, and the discharge end of described discharging mechanism is connected with blanking mechanism, described
The lower section of blanking structure is provided with the jet mixer being connected with supply line, and described jet mixer is connected with medicament discharge mechanism.
2. Powdered Activated Carbon dry method dosing system as claimed in claim 1 it is characterised in that: described feed mechanism includes vacuum
Feeder, described vacuum feeder is provided with the feeder vacuum tank on the top being arranged on described feed bin, described feeder vacuum tank
Low side be connected with described feeding station, the high-end of described feeder vacuum tank is connected with feeding blower fan.
3. Powdered Activated Carbon dry method dosing system as claimed in claim 2 it is characterised in that: also include source of the gas feed mechanism,
Described source of the gas feed mechanism is connected with feeding station blowback control valve, vacuum tank blowback control valve and cleaner unit blowback control valve, institute
State feeding station blowback control valve, described vacuum tank blowback control valve and described cleaner unit blowback control valve be connected respectively described
Feeding station, described feeder vacuum tank and described roof scrubber；Source of the gas feed mechanism is connected with Arch-Breaking Device air source control valve, institute
State Arch-Breaking Device air source control valve and be connected with the bulkhead Arch-Breaking Device being arranged on described feed bin.
4. Powdered Activated Carbon dry method dosing system as claimed in claim 1 it is characterised in that: described discharging mechanism includes level
The discharge nozzle that direction is arranged and is connected with described discharge valve, one end of described discharge nozzle is provided with discharging machine, described discharging machine
Drive connection has the discharging axle in described discharge nozzle, and described discharging axle is provided with the discharge blade of spiral setting.
5. Powdered Activated Carbon dry method dosing system as claimed in claim 4 it is characterised in that: described discharge valve and described discharging
It is provided with the loose mechanism of discharging, the loose mechanism of described discharging includes the loose axle of horizontally arranged discharging, described discharging between pipe
Loose axle is connected with the loose motor of discharging, and the loose axle of described discharging is provided with pears blade blade.
6. Powdered Activated Carbon dry method dosing system as claimed in claim 4 it is characterised in that: described blanking mechanism includes and goes out
The material blanking tube that the discharge end of expects pipe connects, described material blanking tube vertical direction setting, described material blanking tube is provided with blanking control valve, institute
The lower end stating material blanking tube connects described jet mixer.
7. Powdered Activated Carbon dry method dosing system as claimed in claim 6 it is characterised in that: described material blanking tube be also associated with
The premix barrel that supply line connects, described premix barrel is provided with premix control valve.
8. Powdered Activated Carbon dry method dosing system as claimed in claim 1 it is characterised in that: described medicament discharge mechanism includes and penetrates
The drug discharging tube that stream blender connects, described drug discharging tube is provided with drug control valve.
9. described Powdered Activated Carbon dry method dosing system as arbitrary in claim 1 to 8 it is characterised in that: described blanking mechanism,
The quantity of described jet mixer and described medicament discharge mechanism is respectively two.
10. described Powdered Activated Carbon dry method dosing system as arbitrary in claim 1 to 8 it is characterised in that: described feed bin by under
Supreme it is respectively equipped with lower level-sensing device, middle level-sensing device and high charge level meter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610780839.0A CN106365238A (en) | 2016-08-31 | 2016-08-31 | Powdered activated carbon dry-method feeding system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610780839.0A CN106365238A (en) | 2016-08-31 | 2016-08-31 | Powdered activated carbon dry-method feeding system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106365238A true CN106365238A (en) | 2017-02-01 |
Family
ID=57900341
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610780839.0A Pending CN106365238A (en) | 2016-08-31 | 2016-08-31 | Powdered activated carbon dry-method feeding system |
Country Status (1)
| Country | Link |
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| CN (1) | CN106365238A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108017111A (en) * | 2017-12-26 | 2018-05-11 | 北京北方节能环保有限公司 | Dust active carbon automatic Dosing System |
| CN108382878A (en) * | 2018-03-28 | 2018-08-10 | 天津市艾盟科技发展有限公司 | Movable powder jet automatic continuous feeding equipment |
| CN111939781A (en) * | 2020-08-13 | 2020-11-17 | 廊坊市金来源环保科技有限公司 | Novel jet flow mixing system |
| CN113385091A (en) * | 2021-06-11 | 2021-09-14 | 天津市艾盟科技发展有限公司 | Continuous powder lime forced dispersion and uniform mixing feeding system |
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| CN201737731U (en) * | 2010-07-08 | 2011-02-09 | 湖南华亿市政工程设计有限公司 | Powdered activated carbon dry feeder |
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| CN102992436A (en) * | 2012-11-12 | 2013-03-27 | 奥卡威科技（大连）有限公司 | Movable multi-spiral high-precision activated carbon adding device |
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| Title |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108017111A (en) * | 2017-12-26 | 2018-05-11 | 北京北方节能环保有限公司 | Dust active carbon automatic Dosing System |
| CN108382878A (en) * | 2018-03-28 | 2018-08-10 | 天津市艾盟科技发展有限公司 | Movable powder jet automatic continuous feeding equipment |
| CN111939781A (en) * | 2020-08-13 | 2020-11-17 | 廊坊市金来源环保科技有限公司 | Novel jet flow mixing system |
| CN113385091A (en) * | 2021-06-11 | 2021-09-14 | 天津市艾盟科技发展有限公司 | Continuous powder lime forced dispersion and uniform mixing feeding system |
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Application publication date: 20170201 |
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