CN202506323U - Dry powder liquid drug configuration machine - Google Patents
Dry powder liquid drug configuration machine Download PDFInfo
- Publication number
- CN202506323U CN202506323U CN2012201188349U CN201220118834U CN202506323U CN 202506323 U CN202506323 U CN 202506323U CN 2012201188349 U CN2012201188349 U CN 2012201188349U CN 201220118834 U CN201220118834 U CN 201220118834U CN 202506323 U CN202506323 U CN 202506323U
- Authority
- CN
- China
- Prior art keywords
- dry powder
- water inlet
- inlet pipe
- turbine flowmeter
- dissolving tank
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000843 powder Substances 0.000 title claims abstract description 25
- 239000007788 liquid Substances 0.000 title claims abstract description 13
- 239000003814 drug Substances 0.000 title abstract 3
- 229940079593 drug Drugs 0.000 title abstract 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 26
- 238000002360 preparation method Methods 0.000 claims abstract description 17
- 235000014347 soups Nutrition 0.000 claims description 11
- 230000001939 inductive effect Effects 0.000 claims description 4
- 230000008054 signal transmission Effects 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 5
- 230000005587 bubbling Effects 0.000 abstract description 4
- 230000005540 biological transmission Effects 0.000 abstract 1
- 238000004088 simulation Methods 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
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Abstract
The utility model discloses a dry powder liquid drug configuration machine which comprises an water inlet pipe, a dissolving pool, a driving motor and a spiral feeding machine, wherein the spiral feeding machine is controlled by the driving motor; the dissolving pool is divided into a preparation box, a drug containing box and a storage box which are communicated sequentially; the water inlet pipe is communicated with the preparation box; the spiral feeding machine is communicated with the preparation box; a liquid outlet valve is arranged at the bottom outside the dissolving pool; a turbine flowmeter is arranged on the water inlet pipe and is in transmission connection with a signal of a frequency converter of the driving motor; and the turbine flowmeter detects and outputs a simulation-controlled current signal of 4 to 20 mA to the frequency converter of the driving motor. According to the utility model, the feeding quantity of dry powder is changed synchronously with the size of the signal output by the turbine flowmeter installed at a water inlet, so that the preset concentration of the dry powder is maintained; and a mechanical agitating type is changed into a compressed air bottom bubbling type, so that the dry powder can be dissolved and cured quickly and sufficiently to achieve the best dissolving effect.
Description
Technical field
The utility model relates to a kind of dry powder soup configuration machine, is a kind of equipment that disposes to flocculant PAM in the water treatment.
Background technology
In the water treatment procedure, need be the flocculant of powdery, configuration need be dissolved in water, and stirred according to a certain percentage, carry out slaking again after, could use.Configuration technology in the past, owing to receive the influence of water pressure fluctuations, the water yield can be suddenly big or suddenly small, with a constant dry powder dosage, the concentration of configuration soup is unstable, does not reach technological requirement, has influenced the result of water treatment.In addition, mechanical agitator is not very good to the material mixing effect yet, and caking phenomenon is arranged often, and consuming time longer.
The utility model content
The technical problem that the utility model will solve is: unstable for the liquor strength that overcomes existing Process configuration, as to influence water treatment result problem; A kind of dry powder soup configuration machine is provided; Can set the dosage of dry powder according to the size of discharge; Keep preset concentration, the water treatment effect is very good.
The utility model solves the technical scheme that its technical problem adopted: a kind of dry powder soup configuration machine; Comprise water inlet pipe, dissolving tank, drive motors and feed screw, drive motors control feed screw, dissolving tank are split into the preparation case that communicates successively, molten medicine-chest and storage bin; Water inlet pipe is communicated with the preparation case; Feed screw is communicated with the preparation case, and the dissolving tank outer bottom is provided with liquid valve, it is characterized in that: described water inlet pipe is provided with turbine flowmeter; Turbine flowmeter is connected with the frequency converter signal transmission of drive motors, and turbine flowmeter detects and export the frequency converter of the control analog current signal of a 4-20mA to drive motors.
Described preparation case and molten medicine-chest inner bottom part are provided with compressed air hose.
Described dissolving tank inner bottom part and top are provided with the liquid level inductive switch.
Described dissolving tank outer bottom is provided with exhaust-valve.
The beneficial effect of the utility model is: the utility model has been installed turbine flowmeter in the water inlet through design and installation again, comes the dosage of synchronous change dry powder with the output signal magnitude of flowmeter, with the concentration that keeps presetting; Make mechanical agitation type into compressed air bottom bubble type, can make the rapidly sufficient dissolving, curing of medicinal powder, can make solute effect reach optimum state.
Description of drawings
Fig. 1 is the utility model structural representation.
Among the figure: 1. water inlet pipe, 2. hand sluice valve, 3. Pressure gauge, 4. pressure-reducing valve, 5. magnetic valve, 6. feed screw, 7. turbine flowmeter, 8. the dry powder hopper, 9. the blanking vibrator, 10. level sensor, 11. preparation casees, 12. compressed air hoses, 13. dissolve medicine-chests, 14. storage bins, 15. liquid level inductive switches, 16. exhaust-valves, 17. liquid valves, 18. drive motors.
The specific embodiment
Combine accompanying drawing and specific embodiment now, the utility model is done further detailed explanation.These accompanying drawings are the sketch map of simplification, basic structure of the present invention only is described in a schematic way, so it only show the formation relevant with the present invention.
As shown in Figure 1, a kind of dry powder soup configuration machine comprises water inlet pipe 1, dissolving tank, drive motors 18 and feed screw 6; Drive motors 18 control feed screws 6; Feed screw 6 tops are provided with dry powder hopper 8, and dry powder hopper 8 is provided with blanking vibrator 9 and level sensor 10, and dissolving tank is split into the preparation case 11 that communicates successively, molten medicine-chest 13 and storage bin 14; Water inlet pipe 1 is communicated with preparation case 11; Feed screw 6 is communicated with preparation case 11, and the dissolving tank outer bottom is provided with liquid valve 17 and exhaust-valve 16, is provided with hand sluice valve 2, Pressure gauge 3, pressure-reducing valve 4, magnetic valve 5 and turbine flowmeter 7 on the described water inlet pipe 1 successively; Turbine flowmeter 7 is connected with the frequency converter signal transmission of drive motors 18; Turbine flowmeter 7 detects the frequency converter that the control analog current signal of also exporting a 4-20mA is given drive motors, and the rotating speed of drive motors is controlled and changed to frequency converter according to the size of current of accepting, and then drives feed screw 6 and add dry powder.
Behind power connection, open hand sluice valve 2 and magnetic valve 5, current get into dissolving tank through the water pipe of turbine flowmeter 7; 7 of turbine flowmeters can detect this signal; And export the control analog current of a 4-20mA immediately, the frequency converter of drive motors 18 receives this signal, according to the size of electric current; Change the rotating speed of drive motors 18, and drive feed screw 6 adds dry powder.When the hydraulic pressure high flow capacity was big, the signal of turbine flowmeter 7 outputs was just big, and the drive motors rotating speed is just high, and the dry powder dosage is just big, and vice versa.The concentration of its configuration is consistent with the concentration of setting all the time.When accident is cut off the water, then no signal output of turbine flowmeter, conveying worm quits work.
As shown in Figure 1, preparation case 11 is provided with compressed air hose 12 with molten medicine-chest 13 inner bottom parts, and the liquid of dissolving tank is carried out bubbling; Utilize the come-up motion of compressed air at underwater bubble; Vibrations and explosion make medicinal powder dissolving and slaking rapidly, to reach splendid solute effect.After water and flocculant added preparation case 11 simultaneously, and compressed air carries out the bubbling dissolving to it, liquid overflowed into and dissolves medicine-chest 13, and compressed air continues bubbling again, carry out dissolving, curing after, it is subsequent use like storage bin 14 to overflow.
As shown in Figure 1, dissolving tank inner bottom part and top are provided with liquid level inductive switch 15, control the configuration with soup that adds of dosing respectively, emptyly beat or overflow to be unlikely to produce.
Claims (4)
1. dry powder soup configuration machine; Comprise water inlet pipe, dissolving tank, drive motors and feed screw, drive motors control feed screw, dissolving tank are split into the preparation case that communicates successively, molten medicine-chest and storage bin; Water inlet pipe is communicated with the preparation case; Feed screw is communicated with the preparation case, and the dissolving tank outer bottom is provided with liquid valve, it is characterized in that: described water inlet pipe is provided with turbine flowmeter; Turbine flowmeter is connected with the frequency converter signal transmission of drive motors, and turbine flowmeter detects and export the frequency converter of the control analog current signal of a 4-20mA to drive motors.
2. dry powder soup configuration machine according to claim 1 is characterized in that: described preparation case and molten medicine-chest inner bottom part are provided with compressed air hose.
3. dry powder soup configuration machine according to claim 2 is characterized in that: described dissolving tank inner bottom part and top are provided with the liquid level inductive switch.
4. dry powder soup configuration machine according to claim 1 is characterized in that: described dissolving tank outer bottom is provided with exhaust-valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201188349U CN202506323U (en) | 2012-03-27 | 2012-03-27 | Dry powder liquid drug configuration machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201188349U CN202506323U (en) | 2012-03-27 | 2012-03-27 | Dry powder liquid drug configuration machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202506323U true CN202506323U (en) | 2012-10-31 |
Family
ID=47058831
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012201188349U Expired - Fee Related CN202506323U (en) | 2012-03-27 | 2012-03-27 | Dry powder liquid drug configuration machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202506323U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105475943A (en) * | 2015-12-25 | 2016-04-13 | 抚顺市独凤轩食品有限公司 | Full-automatic bone soup making machine |
| CN108421488A (en) * | 2018-05-17 | 2018-08-21 | 昆明冰风科技有限责任公司 | Flocculant automatic dilution and transport system |
| CN114749080A (en) * | 2022-04-20 | 2022-07-15 | 白银新大孚科技化工有限公司 | Automatic flocculant adding system and method |
-
2012
- 2012-03-27 CN CN2012201188349U patent/CN202506323U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105475943A (en) * | 2015-12-25 | 2016-04-13 | 抚顺市独凤轩食品有限公司 | Full-automatic bone soup making machine |
| CN108421488A (en) * | 2018-05-17 | 2018-08-21 | 昆明冰风科技有限责任公司 | Flocculant automatic dilution and transport system |
| CN114749080A (en) * | 2022-04-20 | 2022-07-15 | 白银新大孚科技化工有限公司 | Automatic flocculant adding system and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 201508 Shanghai City, Jinshan District Shanyang town Tingnan No. 3164 Patentee after: Shanghai Weilai Enterprise Co., Ltd. Address before: 201508 Shanghai City, Jinshan District Shanyang town Tingnan No. 3164 Patentee before: Shanghai Weilai Enterprise Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121031 Termination date: 20190327 |