CN206014455U - Powdered Activated Carbon dry method dosing system - Google Patents
Powdered Activated Carbon dry method dosing system Download PDFInfo
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- CN206014455U CN206014455U CN201621010799.3U CN201621010799U CN206014455U CN 206014455 U CN206014455 U CN 206014455U CN 201621010799 U CN201621010799 U CN 201621010799U CN 206014455 U CN206014455 U CN 206014455U
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Abstract
The utility model discloses a kind of Powdered Activated Carbon dry method dosing system, including feeding station, feeding station is connected with feed mechanism, feed bin is connected with below feed mechanism, 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, the discharge end of discharging mechanism is connected with blanking mechanism, is provided with the jet mixer being connected with supply line below blanking structure, and jet mixer is connected with medicament discharge mechanism.Utility model works are stable and reliable for performance, add powder blanking uniform, it is to avoid the flushing of pipeline and blocking, can be operated with whole-course automation, substantially increase production efficiency, reduce human resources, and whole " locked in " operation, it is to avoid cause environmental pollution.
Description
Technical field
The utility model is related to a kind of adding equipment, more particularly to a kind of Powdered Activated Carbon dry method dosing system.
Background technology
Existing 70 years or so the history of use of the Powdered Activated Carbon in Water purification.Since the U.S. is lived using powder first
Property charcoal remove the odor that chlorophenol is produced after, activated carbon become remove in Water purification color, smell, the effective ways of taste and organic matter
One of.The external numerous studies to powder electroless plating performance work show：Powdered Activated Carbon to trichlorophenol, 2,4,6,-T, chlorophenesic acid,
Contained organic matter, haloform and precursor and DBPs trichloroacetic acid, dichloroacetic acid and dihalo- acetonitrile etc. in agricultural chemicals
Deng there is good adsorption effect, check colors, smell, the removal effect of taste is gained public acceptance.
Powdered Activated Carbon is very universal in Europe, the United States, Deng states, 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 is added and is difficult to control to, automatically
Change controlling extent low, due to failing to solve the limitation that the technology is present in application aspect well, it is difficult to play powder activity
The advantage of charcoal technology.
Utility model content
The utility model 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 resources, and whole " locked in " operation, it is to avoid cause ring
The Powdered Activated Carbon dry method dosing system of border pollution.
For solving above-mentioned technical problem, the technical solution of the utility model is：A kind of Powdered Activated Carbon dry method dosing system,
Including feeding station, the feeding station is connected with feed mechanism, is connected with feed bin below the feed mechanism, the feed bin upper
Portion is provided with roof scrubber, and the bottom of the feed bin is provided with discharge valve, and the lower end of the discharge valve is provided with discharging mechanism, described go out
The discharge end of material mechanism is connected with blanking mechanism, is provided with, below the blanking structure, the jet mixing being connected with supply line
Device, the jet mixer are connected with medicament discharge mechanism.
Used as preferred technical scheme, the feed mechanism includes vacuum feeder, and the vacuum feeder is provided with installation
In the feeder vacuum tank on the top of the feed bin, the low side of the feeder vacuum tank is connected with the 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 the source of the gas feed mechanism is connected with feeding station
Control valve, vacuum tank blowback control valve and deduster blowback control valve is blown, the feeding station blowback control valve, the vacuum tank are anti-
Blow control valve and deduster blowback control valve is connected respectively the feeding station, the feeder vacuum tank and the storehouse
Top deduster；Source of the gas feed mechanism is connected with Arch-Breaking Device air source control valve, and the Arch-Breaking Device air source control valve is connected with and is arranged on
Bulkhead Arch-Breaking Device on the feed bin.
Used as the improvement to above-mentioned technical proposal, the discharging mechanism is included horizontally arranged and is connected with the discharge valve
The discharge nozzle for connecing, one end of the discharge nozzle are provided with discharging machine, and the discharging machine drive connection has positioned at the discharge nozzle
Interior discharging axle, the discharging axle are provided with the discharge blade of spiral setting.
As the improvement to above-mentioned technical proposal, the loose mechanism of discharging between the discharge valve and the discharge nozzle, is provided with,
The loose mechanism of the discharging includes the loose axle of horizontally arranged discharging, and the loose axle of the discharging is connected with the loose electricity of discharging
Machine, the loose axle of the discharging are provided with pears blade blade.
Used as the improvement to above-mentioned technical proposal, the blanking mechanism includes the blanking being connected with the discharge end of discharge nozzle
Pipe, the material blanking tube vertical direction are arranged, and the material blanking tube is provided with blanking control valve, and the lower end connection of the material blanking tube is described
Jet mixer.
Used as the further improvement to above-mentioned technical proposal, the material blanking tube is also associated with the premix being connected with supply line
Pipe, the premix barrel are provided with premix control valve.
Used as the further improvement to above-mentioned technical proposal, the medicament discharge mechanism includes the drug being connected with jet mixer
Pipe, the drug discharging tube are provided with drug control valve.
As the further improvement to above-mentioned technical proposal, the blanking mechanism, the jet mixer and the drug
The quantity of mechanism is respectively two.
As the further improvement to above-mentioned technical proposal, the feed bin be respectively equipped with from the bottom to top lower level-sensing device, in
Level-sensing device and high charge level meter.
As a result of above-mentioned technical proposal, a kind of Powdered Activated Carbon dry method dosing system, including feeding station, feeding station connects
Feed mechanism is connected to, feed bin below feed mechanism, is connected with, 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 are provided with discharging mechanism, and the discharge end of discharging mechanism is connected with blanking mechanism, the lower section of blanking structure
The jet mixer being connected with supply line is provided with, jet mixer is connected with medicament discharge mechanism.Packed Powdered Activated Carbon is passed through
Feeding station is poured into after artificial unpacking, starts feed mechanism and roof scrubber, powder is transported to feed bin in feeding station.Add
When, discharge valve, discharging mechanism and blanking mechanism to be opened, makes blanking channel smooth, water is mixed by jet mixer with Powdered Activated Carbon
After conjunction, jet is added to toss area to medicament discharge mechanism.Utility model works are stable and reliable for performance, add powder blanking uniformly,
The flushing and blocking of pipeline is avoided, can be operated with whole-course automation, be substantially increased production efficiency, reduce human resources,
And whole " locked in " operation, it is to avoid cause environmental pollution.
Description of the drawings
The following drawings is only intended to, in the utility model is done schematic illustration and explanation, not limit model of the present utility model
Enclose.Wherein：
Fig. 1 is the structural representation of the utility model embodiment one；
Fig. 2 is the structure principle chart in the A portions of the utility model embodiment one；
Fig. 3 is the structural representation of the utility model embodiment two.
In figure：1- feeding stations；21- feeder vacuum tanks；22- feeding blower fans；3- feed bins；31- discharge valves；Material position under 32-
Meter；Level-sensing device in 33-；34- high charge level meters；35- roof scrubbers；4- discharge nozzles；41- discharging machines；42- discharging loosening machines
Structure；5- blanking mechanisms；51- material blanking tubes；52- blanking control valves；53- premix barrels；54- premix control valves；55- jet mixers；
61- source of the gas feed mechanisms；The blowback of 62- feeding stations controls valve；The blowback of 63- vacuum tanks controls valve；The blowback of 64- dedusters controls valve；
65- Arch-Breaking Device air source control valves；66- bulkhead Arch-Breaking Devices；7- drug discharging tubes；71- drugs control valve；8- supply lines.
Specific embodiment
With reference to the accompanying drawings and examples, the utility model is expanded on further.In the following detailed description, only by saying
Bright mode describes some one exemplary embodiments of the present utility model.Undoubtedly, one of ordinary skill in the art can be with
Recognize, in the case of without departing from spirit and scope of the present utility model, can with a variety of modes to described
Embodiment is modified.Therefore, accompanying drawing and description are inherently illustrative, rather than for limiting the protection of claim
Scope.
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, is connected with feed bin 3 below feed mechanism, 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 jet mixer 55 being connected with supply line 8 is provided with below blanking structure, 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, discharge valve 31, discharging mechanism and blanking mechanism 5 is opened, makes blanking channel smooth, jet
Blender 55 water is mixed with Powdered Activated Carbon after jet to medicament discharge mechanism, be added to toss area.
Utility model feed mechanism includes that vacuum feeder, utility model vacuum feeder are provided with installed in utility model material
The feeder vacuum tank 21 on the top in storehouse 3, the low side of utility model feeder vacuum tank 21 are connected with utility model feeding station 1,
The high-end of utility model feeder vacuum tank 21 is connected with feeding blower fan 22.Set between the vacuum feeder suction blanking time
Every, utility model feeding blower fan 22 is opened, generation negative pressure in utility model feeder vacuum tank 21, in utility model feeding station 1
Powdered Activated Carbon be inhaled in utility model feeder vacuum tank 21, when utility model feeding blower fan 22 quits work, real
Dropped in feed bin 3 with the Powdered Activated Carbon in novel loading machine vacuum tank 21, said structure can realize automatic charging, closed
Conveying, prevents dust from flying, time saving and energy saving.
Also include source of the gas feed mechanism 61, utility model source of the gas feed mechanism 61 be connected with feeding station blowback control valve 62,
Vacuum tank blowback control valve 63 and deduster blowback control valve 64, utility model feeding station blowback control valve 62, utility model are true
Slack tank blowback control valve 63 and utility model deduster blowback control valve 64 are connected respectively utility model feeding station 1, practicality
Novel loading machine vacuum tank 21 and utility model roof scrubber 35；Source of the gas feed mechanism 61 is connected with Arch-Breaking Device air source control valve
65, utility model Arch-Breaking Device air source control valve 65 is connected with the bulkhead Arch-Breaking Device 66 on utility model feed bin 3.
Source of the gas feed mechanism 61 provides gas, controls the keying that feeding station blowback controls valve 62, can realize to feeding station 1
Carry out blowback, it is to avoid Powdered Activated Carbon accumulated plugging in the feeding station 1；The blowback of control vacuum tank controls the keying of valve 63, can
Realize carrying out blowback to feeder vacuum tank 21, it is to avoid Powdered Activated Carbon accumulated plugging in the feeder vacuum tank 21；Control is removed
The blowback of dirt device controls the keying of valve 64, can realize carrying out blowback to roof scrubber 35, it is to avoid Powdered Activated Carbon is removed in silo roof
Accumulated plugging in dirt device 35；The keying of control Arch-Breaking Device air source control valve 65, can make 66 action of bulkhead Arch-Breaking Device, it is to avoid powder
Activated carbon accumulated plugging in the utility model feed bin 3, and hole shakes, and efficient broken arch effectively prevents powder cavity, improves and throw
Material accuracy.
Source of the gas feed mechanism 61 can include that air compressor, air compressor connect air accumulator, and air accumulator connection is free
Gas drying machine, finally transfers out pressure and the satisfactory source of the gas of humidity by dried-air drier.
Utility model discharging mechanism includes discharge nozzle 4 that is horizontally arranged and being connected with utility model discharge valve 31, real
Discharging machine 41 is provided with one end of novel discharging pipe 4,41 drive connection of utility model discharging machine has to go out positioned at utility model
Discharging axle in expects pipe 4, utility model discharging axle are provided with the discharge blade of spiral setting.Utility model discharge valve 31 is opened,
Powdered Activated Carbon in utility model feed bin 3 is dropped in discharge nozzle 4, and the work of discharging machine 41 drives discharging axle and discharging leaf
Piece, makes Powdered Activated Carbon move to 4 discharge end of discharge nozzle in discharge nozzle 4.Utility model discharging machine 41 be variable-frequency motor, energy
Discharging speed, control discharging speed are enough adjusted.
The loose mechanism 42 of discharging is provided between utility model discharge valve 31 and utility model discharge nozzle 4, and utility model discharges
Loose mechanism 42 includes that the loose axle of horizontally arranged discharging, the loose axle of utility model discharging are connected with the loose motor of discharging,
The loose axle of utility model discharging is provided with pears blade blade.During discharging, the loose motor of utility model discharging drives out
Expect loose axle and pears blade blade, Powdered Activated Carbon is stirred, fluffing action well can be played, it is to avoid powder is piled up
Blocking.
Utility model blanking mechanism 5 includes the material blanking tube 51 being connected with the discharge end of discharge nozzle 4, utility model material blanking tube 51
Vertical direction is arranged, and utility model material blanking tube 51 is provided with blanking control valve 52, and the lower end connection of utility model material blanking tube 51 is real
With novel jet flow blender 55.Blanking control valve 52 is opened, the Powdered Activated Carbon transferred out by utility model discharge nozzle 4 is dropped into
Material blanking tube 51, it is ensured that Powdered Activated Carbon is transported to jet mixer 55.
Utility model material blanking tube 51 is also associated with the premix barrel 53 being connected with supply line 8, in utility model premix barrel 53
Premix control valve 54 is provided with, premix control valve 54 is opened, can be allowed water to flow in premix barrel 53, Powdered Activated Carbon is premixed,
Then jet mixer 55 is transported to again.
Utility model medicament discharge mechanism includes that the drug discharging tube 7 being connected with jet mixer 55, utility model drug discharging tube 7 are provided with
Drug controls valve 71, and said structure conveniently can be controlled.
Utility model feed bin 3 is respectively equipped with lower level-sensing device 32, middle level-sensing device 33 and high charge level meter 34, lower material position from the bottom to top
Meter 32, middle level-sensing device 33 and high charge level meter 34 are connected with PLC control cabinet, and lower 32 detection signal of level-sensing device, when Powdered Activated Carbon position
When lower level-sensing device is below 32, reports to the police and stop utility model discharging mechanism helical feed；33 detection signal of middle level-sensing device, works as powder
Activated carbon is located at below middle material position and during lower level-sensing device more than 32, reminds feeding；34 detection signal of high charge level meter, works as powder activity
When charcoal is higher than high charge level meter 34, reports to the police and limit feeding.
Certainly PLC can also control to connect each motor and control valve, can realize 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, can be with
Whole-course automation is operated, and substantially increases production efficiency, reduces human resources, and whole " locked in " operation, it is to avoid cause ring
Pollute in border.
Embodiment two：As shown in figure 3, embodiment two is with the difference of embodiment one, utility model blanking mechanism
5th, the quantity of utility model jet mixer 55 and utility model medicament discharge mechanism is respectively two, two utility model blanking mechanisms
5 can simultaneously blanking, and be respectively delivered to corresponding jet mixer 55, medicament discharge mechanism, realize discharging simultaneously, substantially increase
Operating efficiency.
General principle of the present utility model, principal character and advantage of the present utility model has been shown and described above.One's own profession
The technical staff of industry it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Principle of the present utility model is described simply, on the premise of without departing from the utility model spirit and scope, the utility model is also
Various changes and modifications are had, these changes and improvements are both fallen within the range of claimed the utility model.The utility model
Claimed scope is 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：The feeding station is connected with feeder
Structure, is connected with feed bin below the feed mechanism, the top of the feed bin is provided with roof scrubber, and the bottom of the feed bin sets
The lower end for having discharge valve, the discharge valve is provided with discharging mechanism, and the discharge end of the discharging mechanism is connected with blanking mechanism, described
The jet mixer being connected with supply line is provided with below blanking structure, and the 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：The feed mechanism includes vacuum
Feeder, the vacuum feeder are provided with the feeder vacuum tank installed in the top of the feed bin, the feeder vacuum tank
Low side be connected with the feeding station, the high-end of the 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,
The source of the gas feed mechanism is connected with feeding station blowback control valve, vacuum tank blowback control valve and deduster blowback control valve, institute
State feeding station blowback control valve, vacuum tank blowback control valve and deduster blowback control valve be connected respectively described
Feeding station, the feeder vacuum tank and the roof scrubber；Source of the gas feed mechanism is connected with Arch-Breaking Device air source control valve, institute
State the bulkhead Arch-Breaking Device that Arch-Breaking Device air source control valve is connected with the feed bin.
4. Powdered Activated Carbon dry method dosing system as claimed in claim 1, it is characterised in that：The discharging mechanism includes level
The discharge nozzle that direction is arranged and is connected with the discharge valve, one end of the discharge nozzle are provided with discharging machine, the discharging machine
Drive connection has the discharging axle in the discharge nozzle, the discharging axle to be 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：The discharge valve and the discharging
It is provided with the loose mechanism of discharging between pipe, the loose mechanism of the discharging includes the loose axle of horizontally arranged discharging, the discharging
Loose axle is connected with the loose motor of discharging, and the loose axle of the 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：The blanking mechanism includes and goes out
The material blanking tube of the discharge end connection of expects pipe, the material blanking tube vertical direction are arranged, and the material blanking tube is provided with blanking control valve, institute
The lower end for stating material blanking tube connects the jet mixer.
7. Powdered Activated Carbon dry method dosing system as claimed in claim 6, it is characterised in that：The material blanking tube be also associated with
The premix barrel of supply line connection, the premix barrel are provided with premix control valve.
8. Powdered Activated Carbon dry method dosing system as claimed in claim 1, it is characterised in that：The medicament discharge mechanism includes and penetrates
The drug discharging tube of stream blender connection, the drug discharging tube are provided with drug control valve.
9. the Powdered Activated Carbon dry method dosing system as described in claim 1 to 8 is arbitrary, it is characterised in that：The blanking mechanism,
The quantity of the jet mixer and the medicament discharge mechanism is respectively two.
10. the Powdered Activated Carbon dry method dosing system as described in claim 1 to 8 is arbitrary, it is characterised in that：The feed bin is 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 |
|---|---|---|---|
| CN201621010799.3U CN206014455U (en) | 2016-08-31 | 2016-08-31 | Powdered Activated Carbon dry method dosing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621010799.3U CN206014455U (en) | 2016-08-31 | 2016-08-31 | Powdered Activated Carbon dry method dosing system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206014455U true CN206014455U (en) | 2017-03-15 |
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ID=58256391
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621010799.3U Active CN206014455U (en) | 2016-08-31 | 2016-08-31 | Powdered Activated Carbon dry method dosing system |
Country Status (1)
| Country | Link |
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| CN (1) | CN206014455U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
-
2016
- 2016-08-31 CN CN201621010799.3U patent/CN206014455U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |