CN103411135A - Positive-negative double-acting bubble removing and rapid conveying device for starch slurry - Google Patents
Positive-negative double-acting bubble removing and rapid conveying device for starch slurry Download PDFInfo
- Publication number
- CN103411135A CN103411135A CN2013103497492A CN201310349749A CN103411135A CN 103411135 A CN103411135 A CN 103411135A CN 2013103497492 A CN2013103497492 A CN 2013103497492A CN 201310349749 A CN201310349749 A CN 201310349749A CN 103411135 A CN103411135 A CN 103411135A
- Authority
- CN
- China
- Prior art keywords
- tank
- vacuum
- slurry
- solenoid valve
- vacuum 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.)
- Granted
Links
- 239000002002 slurry Substances 0.000 title claims abstract description 38
- 229920002472 Starch Polymers 0.000 title abstract description 7
- 235000019698 starch Nutrition 0.000 title abstract description 7
- 239000008107 starch Substances 0.000 title abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 125000004122 cyclic group Chemical group 0.000 claims description 15
- 239000010865 sewage Substances 0.000 claims description 9
- 238000004513 sizing Methods 0.000 claims description 5
- 238000005553 drilling Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 12
- 230000002349 favourable effect Effects 0.000 abstract description 2
- 239000013642 negative control Substances 0.000 abstract 1
- 239000013641 positive control Substances 0.000 abstract 1
- 238000005086 pumping Methods 0.000 abstract 1
- 239000003570 air Substances 0.000 description 34
- 238000007599 discharging Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 238000009411 base construction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229920001592 potato starch Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000009955 starching Methods 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
Images
Landscapes
- Paper (AREA)
Abstract
The invention discloses a positive-negative double-acting bubble removing and rapid conveying device for starch slurry. The bubble removing and rapid conveying device is composed of a vacuum tank, a vacuum pump, a circulation water tank, an air compressor, a slurry tank and matched attachments such as process valves and pipelines. The vacuum pump and the air compressor are used for positive and negative control, bubbles in the slurry are effectively sucked out through vacuum pumping, and the slurry is conveyed to a production producing line rapidly through positive pressure generated by the air compressor. The device is automatically controlled through solenoid valves, operation time for production is shortened, the labor intensity of operators is reduced, the product quality is improved, and favorable conditions are created for selling products and wining markets.
Description
Technical field
The present invention relates to a kind of system and device of quick conveying slurry, is a kind of bubble that affects quality of product in the starchiness slurry, device that slurry is delivered to fast to production and processing line can effectively removed in starch is sized mixing process specifically.
Background technique
Fast development along with the Dingxi, Gansu Potato Industry, rely on the leading enterprise such as industrial base construction, processing, sale of local natural resource advantages arise at the historic moment and form fairly largely, especially as the potato starch product processing enterprise of high added value, be surging forward in various places.At present, when the manufacturing enterprise of starch-based product processing produces, all will be through the size mixing technology of starch bearing material, the process Air of sizing mixing is mingled with wherein, the starchiness slurry can form a large amount of bubbles, be difficult to effective removal, having a strong impact on the market sale of quality of product and product, become the difficult problem of puzzlement starch-based product enterprise.
Summary of the invention
In order to address the above problem, the object of the present invention is to provide a kind of starchiness slurry positive/negative-pressure double-action to remove the quick feedway of bubble.Utilize this device can effectively remove the bubble that starch is sized mixing in process and produced, can fast slurry be delivered to the device of production and processing line again.
To achieve these goals, the present invention adopts following technological scheme:
The quick feedway of bubble is removed in a kind of starchiness slurry positive/negative-pressure double-action, mainly comprises: vacuum tank, vacuum pump, cyclic water tank, air compressor, finished pulp batch can.The vacuum tank side-wall hole, by the negative pressure supply pipe, be connected with the tank of sizing mixing with electronic dish valve, the vacuum tank bottom opening is connected with the finished pulp batch can by the mortor operated valve on pipeline, discharge port, and finished pulp batch can bottom is provided with the 5# solenoid valve, and another sidewall of vacuum tank arranges manhole; Isolating plate is set in vacuum tank, seal ring is installed around isolating plate; One-way valve is housed on isolating plate; Telescopic spring is set between vacuum tank inner tip and isolating plate; Vacuum pump is inhaled vacuum interface and is connected vacuum tank top drilling and vacuum tank are airtight by aspirating air pipe, 3# solenoid valve, check valve, the outlet of vacuum pump air water is connected with cyclic water tank, the vacuum pump water intake is connected with cyclic water tank by pipeline by the 4# solenoid valve, and the cyclic water tank bottom is provided with sewage draining exit; Air compressor is by airduct, air filter, and the 1# solenoid valve is connected with the vacuum tank top is airtight, and pipeline is established the quick air inlet of bypass and is provided with the 2# solenoid valve; The air filter bottom is equipped with the air compressor sewage draining exit.
Advantage major embodiment of the present invention is in the following areas:
1, utilize vacuum pump and air compressor positive/negative-pressure to control, the negative pressure of utilizing vacuum pump to produce in the starchiness slurry be delivered to rapidly a certain amount of in vacuum tank after, close feeding valve, and continue to vacuumize the bubble sucking-off effectively be mingled with in slurry.After the exhaustion of starching interior bubble, the malleation that the recycling air compressor system produces is delivered to production and processing line fast by slurry, has improved quality of product, for production marketing has been created more favourable condition with winning the market.
2, realized that the starchiness slurry is stirred, carried without leakage, the automatic control of pollution-free solenoid valve and strength by the omnidistance machinery-free of processing to production line of sizing mixing, and is very easy to production.
The positive/negative-pressure double-action continuous operation principle of the malleation quickly discharging that the negative pressure quick feeding 3, produced by vacuum pump and air compressor produce, realized slurry carry and the production process such as vacuum suction bubble in quick conveying, improved manufacturing efficiency.
4, system all adopts electronic, solenoid valve automatically to control, and has shortened the operating time of production work, has alleviated operator's labor intensity.
The accompanying drawing explanation
Fig. 1 is schematic diagram of the present invention.
In figure: 1-empty compressor 2-negative pressure supply pipe, 3-electric butterfly valve, 4-vacuum tank, 5-isolating plate, 6-flexible springs 7---1# solenoid valve, 8-2# solenoid valve, 9-3# solenoid valve, 15-4# solenoid valve, 19-5# solenoid valve, 10-check valve, 11-manhole, 12-one-way valve, 13-seal ring, 14-cyclic water tank, 16-sewage draining exit, 17-vacuum pump, 18-finished pulp batch can, 19-5# solenoid valve, 20-discharge port, 21-mortor operated valve, 22-air compressor sewage draining exit, 23-air filter.
Embodiment
Below, by reference to the accompanying drawings technical solution of the present invention is described further again:
As shown in Figure 1, the quick feedway of bubble is removed in a kind of starchiness slurry positive/negative-pressure double-action, mainly comprises: the annexes such as the technique valve of vacuum tank 4, vacuum pump 15, cyclic water tank 14, air compressor 1, slurry tank 18 5 major parts and supporting installation, pipeline form.Slurry tank 16, vacuum tank 4 side-wall holes, by negative pressure supply pipe 2, be connected with the tank of sizing mixing with electronic dish valve 3, vacuum tank 4 bottom opening are connected with finished pulp batch can 18 by mortor operated valve on pipeline 21, discharge port 20, and finished pulp batch can 18 bottoms are provided with 5# solenoid valve 19.For the ease of maintenance, at vacuum tank 4 another sidewalls, manhole 11 is set; Isolating plate 5 is set in tank, and isolating plate 5 peripheries are installed seal ring 13; And one-way valve 12 is housed on isolating plate 5.One-way valve 12 is opened when inhaling vacuum.While just compressing into air, one-way valve 12 is closed, and while having realized malleation conveying slurry, slurry and air compressor gas is effectively isolated.For isolating plate 5 can need to be moved up and down with production technology, telescopic spring 6 is set between tank interior top and isolating plate 5.
Air compressor 1 exhausts after bubble the quick feedway of power that is delivered to fast finished pulp batch can 18 for the slurry vacuum.Air compressor 1 passes through airduct, air filter 23,1# solenoid valve 7 and airtight connection of vacuum tank 4 tops, and for tank internal pressure after making in vacuum tank 4 to take out most bubble returns normal pressure, pipeline is established the quick air inlet of bypass and is controlled by 2# solenoid valve 8; In order to guarantee the technique air cleaning, air filter 23 is set on pipeline; In order regularly to discharge impurity, air compressor sewage draining exit 22. is established in air filter 23 bottoms
Finished pulp batch can 18 is the temporary storage appts. for slurry to be processed after suction vacuum removal bubble, with the supporting setting of production and processing line.
During operation, the present invention operates by following technological process:
1, each equipment valve of check system normal operation whether, before the system operation, each equipment all stops, and each valve all is in closed condition;
2, in cyclic water tank 14, fill with the technique tap water, open negative pressure supply pipe 2, electric butterfly valve 3, vacuum tank 1# solenoid valve, vacuum cycle water pipe 3# solenoid valve;
3, start vacuum pump 17, the negative pressure of utilizing vacuum to produce is drawn to the modulated slurry made in vacuum tank 4, after the interior slurry of vacuum tank 4 reaches prearranging quatity, close negative pressure supply pipe electric butterfly valve 3, after this valve cuts out, continue to use vacuum pump 17 to vacuumize, treat that degree of vacuum reaches-0.76Mpa, when in slurry, the bubble residual capacity does not affect quality of product, close vacuum pump 17, close negative-pressure vacuum pipe 4# solenoid valve;
4, open vacuum tank top bypass air compressor 2# solenoid valve 8, when vacuum tank 4 internal air pressures and barometric pressure balance each other, close 2# solenoid valve 8.Open subsequently air compressor air intake pipe 1# solenoid valve 7, open vacuum tank discharging mortor operated valve 21 and carry out the preparation of reception slurry;
5, open air compressor 1, inject to vacuum tank 4 clean air filtered, under the effect of spring 6, to lower compression, force slurry from the interior quick discharge of slurry tank 18 isolating plate 5;
6, after the slurry of slurry tank 18 drains, close the 1# solenoid valve on air compressor 1 and inlet pipe, close discharge port electric butterfly valve 21, vacuum degassing bubble positive/negative-pressure slurry quick conveyance system completes a work cycle.
Claims (1)
1. the quick feedway of bubble is removed in a starchiness slurry positive/negative-pressure double-action, mainly comprise: vacuum tank (4), vacuum pump (15), cyclic water tank (14), air compressor (1), slurry tank (18), it is characterized in that vacuum tank (4) side-wall hole, by negative pressure supply pipe (2), be connected with the tank of sizing mixing with electronic dish valve (3), vacuum tank (4) bottom opening is by the mortor operated valve on pipeline (21), discharge port (20) is connected with finished pulp batch can (18), slurry tank (18) bottom is provided with 5# solenoid valve (19), another sidewall of vacuum tank (4) arranges manhole door (11), isolating plate (5) is set in vacuum tank (4), and isolating plate (5) is installed seal ring (13) on every side, one-way valve (12) is housed on isolating plate (5), between vacuum tank (4) inner tip and isolating plate (5), telescopic spring (6) is set, vacuum pump (17) is inhaled vacuum interface and is passed through aspirating air pipe, 3# solenoid valve (9), check valve (10) in vacuum tank top drilling and airtight connection of vacuum tank (4), the outlet of vacuum pump (17) air water is connected with cyclic water tank (14), vacuum pump (17) water intake is connected with cyclic water tank (14) by pipeline by 4# solenoid valve (15), and cyclic water tank (14) bottom is provided with sewage draining exit (16), air compressor (1) passes through airduct, air filter (23), 1# solenoid valve (7) and vacuum tank (4) the airtight connection of top, and pipeline is established the quick air inlet of bypass and is provided with 2# solenoid valve (8), air filter (23) bottom is equipped with air compressor sewage draining exit (22).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310349749.2A CN103411135B (en) | 2013-08-13 | 2013-08-13 | The quick feedway of bubble is removed in the double-action of a kind of starchiness slurry positive/negative-pressure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310349749.2A CN103411135B (en) | 2013-08-13 | 2013-08-13 | The quick feedway of bubble is removed in the double-action of a kind of starchiness slurry positive/negative-pressure |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103411135A true CN103411135A (en) | 2013-11-27 |
| CN103411135B CN103411135B (en) | 2015-10-14 |
Family
ID=49604164
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310349749.2A Expired - Fee Related CN103411135B (en) | 2013-08-13 | 2013-08-13 | The quick feedway of bubble is removed in the double-action of a kind of starchiness slurry positive/negative-pressure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103411135B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111024912A (en) * | 2019-12-27 | 2020-04-17 | 重庆国环绿源科技有限公司 | Ship wastewater pretreatment type detection device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5832948A (en) * | 1996-12-20 | 1998-11-10 | Chemand Corp. | Liquid transfer system |
| CN201293204Y (en) * | 2009-03-09 | 2009-08-19 | 韩红卫 | Full automatic centralization supplier for liquid auxiliary raw material |
| CN101782181A (en) * | 2009-01-17 | 2010-07-21 | 梁海朋 | Non-contact pneumatic liquid energy-saving conveying device |
| CN202148043U (en) * | 2011-05-31 | 2012-02-22 | 济宁天恒电气设备制造有限公司 | Pneumatic slurry residue conveyor |
| CN102499401A (en) * | 2011-11-11 | 2012-06-20 | 宋贵民 | Vermicelli processing method |
-
2013
- 2013-08-13 CN CN201310349749.2A patent/CN103411135B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5832948A (en) * | 1996-12-20 | 1998-11-10 | Chemand Corp. | Liquid transfer system |
| CN101782181A (en) * | 2009-01-17 | 2010-07-21 | 梁海朋 | Non-contact pneumatic liquid energy-saving conveying device |
| CN201293204Y (en) * | 2009-03-09 | 2009-08-19 | 韩红卫 | Full automatic centralization supplier for liquid auxiliary raw material |
| CN202148043U (en) * | 2011-05-31 | 2012-02-22 | 济宁天恒电气设备制造有限公司 | Pneumatic slurry residue conveyor |
| CN102499401A (en) * | 2011-11-11 | 2012-06-20 | 宋贵民 | Vermicelli processing method |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111024912A (en) * | 2019-12-27 | 2020-04-17 | 重庆国环绿源科技有限公司 | Ship wastewater pretreatment type detection device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103411135B (en) | 2015-10-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201991788U (en) | Self-suction type vacuum water pumping machine | |
| CN204391204U (en) | A kind of slurry processing and automatically feed system | |
| CN103411135A (en) | Positive-negative double-acting bubble removing and rapid conveying device for starch slurry | |
| CN204039048U (en) | A kind of chemical device for discharging | |
| CN103863820B (en) | A kind of material transmission system and material transferring method | |
| CN215250689U (en) | Energy-saving desolventizer-toaster | |
| CN206413722U (en) | The double heavy pond water saving bubble descaling machines of flush-type garlic | |
| CN112483167B (en) | Mine coal slurry cleaning device and use method thereof | |
| CN204656697U (en) | Changing food waste batch process equipment | |
| CN205547281U (en) | Fruit -cleaning machine | |
| CN208699148U (en) | The vacuum-packed blast resistance construction of gas-phase silica | |
| CN204400735U (en) | A kind of bio-pharmaceuticals polluted water pretreatment apparatus | |
| CN209324369U (en) | A kind of vacuum sewerage vertical hoisting system | |
| CN205330989U (en) | Rotary -vane vacuum pump machine oil quick replacement device | |
| CN219558812U (en) | Kitchen garbage thick liquid sand removal device | |
| CN201340179Y (en) | Vacuum conveying device for polyester chip | |
| CN204714073U (en) | A kind of vacuum intaking device | |
| CN104324530A (en) | Waste alcohol sediment separation device for sausage casing residues | |
| CN104888909B (en) | Kitchen waste batch treatment equipment special-purpose crushing device | |
| CN205223016U (en) | Device is prepared to lime breast with water smoke dust removal function | |
| CN204355767U (en) | Nd Fe B alloys powder transmitting device | |
| CN203743016U (en) | Sewage conveying system | |
| CN209997624U (en) | A reactor vacuum nitrogen addition device | |
| CN202209280U (en) | Water pump with self-suction unit | |
| CN108891655A (en) | The vacuum-packed blast resistance construction of gas-phase silica and method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20151014 Termination date: 20160813 |