CN203417608U - Liquid powder mixing machine - Google Patents
Liquid powder mixing machine Download PDFInfo
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- CN203417608U CN203417608U CN201320415342.0U CN201320415342U CN203417608U CN 203417608 U CN203417608 U CN 203417608U CN 201320415342 U CN201320415342 U CN 201320415342U CN 203417608 U CN203417608 U CN 203417608U
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Abstract
The utility model discloses a liquid powder mixing machine which comprises a milk melting tank, a powder melting device, a milk powder bin and a controller, wherein a weighing sensor, a shearing and stirring device and a vacuum control device are arranged in the powder melting device; a feed channel and a discharge channel are arranged between the milk melting tank and the powder melting device; a feed pump and a feed valve are arranged on the feed channel; a discharge pump and a discharge valve are arranged on the discharge channel; a suction channel is arranged between the milk powder bin and the powder melting device; a milk powder suction valve is arranged on the suction channel; and the feed valve, the discharge valve and the milk powder suction valve are connected with the controller respectively. The provided liquid powder mixing machine can dissolve milk powder uniformly.
Description
Technical field
The utility model relates to food processing field, especially relates to a kind of water-powder mixer.
Background technology
At present, in food and drink feed proportioning system, traditional milk powder dissolution equipment is formed by one group of stirrer combination in a melting tank and tank conventionally.As Chinese patent Granted publication number: CN 202105614U, January 11 2012 Granted publication day, a kind of water-powder mixer is disclosed, comprise frame, powder bucket and mixing chamber, described powder bucket is arranged on mixing chamber top and connects with mixing chamber, is provided with rotating shaft and mixing component in described mixing chamber, and described mixing component is fixedly connected with rotating shaft and longitudinally among mixing chamber, described mixing chamber middle part sidewall is provided with liquid material import, and described mixing chamber bottom sidewall is provided with discharging opening.Mixing chamber in this patent is equivalent to milk powder melting tank, in use, in mixing chamber, according to proportioning, adds a certain amount of water, adds the milk powder of proportioning requirement in from powder bucket, and turn on agitator is dissolved milk powder in water.But, while using equipment of the prior art, due to by manually pouring milk powder into, the quantity of pouring milk powder in unit interval into is inhomogeneous, sometimes fast and sometimes slow, when milk powder is poured excessive velocities into, milk powder has little time to dissolve, and caking phenomenon easily occurs, and has therefore greatly affected production quality and mouthfeel.
Utility model content
The utility model is that milk powder dissolves inhomogeneous deficiency in order to overcome in prior art pigment and to mix, and a kind of Water powdery mixer that can realize milk powder uniform dissolution is provided.
To achieve these goals, the utility model is by the following technical solutions:
A kind of water-powder mixer of the present utility model, comprising milk container, change powder device, milk powder storehouse and controller, in described change powder device, be provided with LOAD CELLS, shear agitation device and vacuum control unit, between described change milk container and change powder device, be provided with feeding-passage and tapping channel, described feeding-passage is provided with feed pump and inlet valve, described tapping channel is provided with discharging pump and outlet valve, between described milk powder storehouse and change powder device, be provided with suction passage, described suction passage is provided with milk powder inlet valve, described inlet valve, outlet valve is connected with controller respectively with milk powder inlet valve.In use, add quantitative water and milk powder changing milk container and milk powder storehouse respectively, the water in change milk container by feed pump and inlet valve inputization powder device.Water level in changing powder device arrives specifies after liquid level, and discharging pump and outlet valve are started working, and making milk container and the water of changing in powder device start to circulate.Open milk powder inlet valve suction milk powder, after the milk powder being inhaled into melts, form milk and circulate between change milk container and change powder device.Reach after the circulation timei of technological requirement, feed pump and inlet valve are out of service, and discharging pump, outlet valve continue operation, like this, the liquid level of changing in powder device reduces gradually, until change milk in powder tank all after entering milk container, discharging pump, outlet valve are closed, and whole pigment mixed process all completes.In mixed dissolution process, because water circulates in changing powder device and changing milk container, while milk powder is joining powder device evenly, and milk powder can be dissolved in water rapidly, avoids manually adding the caking phenomenon that milk powder causes, and production efficiency improves.In addition, workman's labour intensity also reduces greatly, and has avoided manual intervention, and the hygienic conditions while making operation improve.
As preferably, stirring clipper and cooling system that described shear agitation device comprises stirring motor, by stirring motor, driven.Like this, milk powder can carry out high-speed stirred shearing after adding, and milk powder dissolved matter particle is diminished, and the quality of product is further enhanced.
As preferably, between described outlet valve and change powder device, be provided with circulation branch road, circulation branch road is provided with circulating valve.During beginning, water, changing milk container and changing circulation time between powder device, can be opened circulating valve, improves circulation rate.When stirring cutter running, circulating valve can cut out, guarantee that the high-speed stirred shearing of stirring cutter fully mixes water and milk powder.
As preferably, described vacuum-control(led) system comprises vacuum sensor, vacuum transducer, vacuum governor, vavuum pump and the vacuum conditions magnetic valve being connected with vavuum pump, described vacuum sensor is connected with vacuum transducer, and described vacuum transducer, vacuum conditions magnetic valve are connected with vacuum governor respectively.Negative pressure of vacuum situation in vacuum sensor detectionization powder device, by vacuum transducer, become and send after conversion, signal is sent to vacuum governor, vacuum governor is according to changing negative pressure of vacuum situation in powder device, control the switching of vacuum conditions magnetic valve, the vacuum degree control of changing in powder device is extremely born between 0.06MPa at negative 0.04MPa, and the vacuum keep homeostasis in making powder device, guarantees that the powder amount sucking is even.Under vacuum state, during high-speed stirred, air can not infiltrated in milk, thereby has reduced the generation of milk foam, is convenient to the accurate control of liquid level when filling.
As preferably, in described milk powder storehouse, be provided with powder position detecting sensor and silo-wall shaker, described powder position detecting sensor is connected respectively at controller with silo-wall shaker.Powder position detecting sensor can provide powder position information for controller, and by silo-wall shaker, guarantees the smooth supply of milk powder, reduces the residual of milk powder.
As preferably, described milk powder inlet valve is connected with inhales powder delay controller.Inhale powder delay controller and can be used for controlizations powder device suction powder time and intermittent time.When powder position reaches predetermined altitude, powder level sensor senses that milk powder and vacuum normally surpass negative 0.04MPa, changes powder device and just can start quantitatively intermittently to inhale powder.
Therefore, the utlity model has following beneficial effect: in (1) unit interval, quantitative and even adds milk powder, and the dissolving of milk powder is comparatively even; (2) milk powder can carry out high-speed stirred shearing after adding, and milk powder dissolves fast, and dissolved matter particle is little; (3) reduce labor strength, enhance productivity and health grade; (4) under vacuum state during high-speed stirred, air can not infiltrated in milk, thereby has reduced the generation of milk foam, is convenient to the accurate control of liquid level when filling.
Accompanying drawing explanation
Fig. 1 is schematic diagram of the present utility model.
In figure, change milk container 1, outlet valve 2, changes powder device 3, inlet valve 4, milk powder storehouse 5, milk powder inlet valve 6, circulating valve 7, discharging pump 8, feed pump 9.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
In embodiment as shown in Figure 1, a kind of water-powder mixer, comprising milk container 1, change powder device 3, milk powder storehouse 5 and controller, change milk container and change between powder device and be provided with feeding-passage and tapping channel, feeding-passage is provided with feed pump 9 and inlet valve 7, and tapping channel is provided with discharging pump 8 and outlet valve 2, between milk powder storehouse and change powder device, is provided with suction passage, suction passage is provided with milk powder inlet valve 3, and inlet valve, outlet valve and milk powder inlet valve are connected with controller respectively.In addition, between outlet valve and change powder device, be provided with circulation branch road, circulation branch road is provided with circulating valve 7.
Change in powder device and be provided with LOAD CELLS, shear agitation device and vacuum control unit, vacuum-control(led) system comprises vacuum sensor, vacuum transducer, vacuum governor, vavuum pump and the vacuum conditions magnetic valve being connected with vavuum pump, vacuum sensor is connected with vacuum transducer, and vacuum transducer, vacuum conditions magnetic valve are connected with vacuum governor respectively.Stirring clipper and cooling system that shear agitation device comprises stirring motor, by stirring motor, driven.In milk powder storehouse, be provided with powder position detecting sensor and silo-wall shaker, powder position detecting sensor is connected respectively at controller with silo-wall shaker, and wherein, milk powder inlet valve is also connected with inhales powder delay controller.
When producing, according to proportioning, add quantitative water and milk powder changing milk container and milk powder storehouse respectively, then changing water in milk container by feed pump and being transported to of inlet valve powder device.Water level in changing powder device arrives specifies after liquid level, and discharging pump and outlet valve are started working, and make water at change milk container and change between powder device to circulate, and the liquid level in making powder device remains on fluctuation in specified scope.When the water level circulation of changing milk container and change between powder device reaches after balance, the shear agitation device of changing powder device brings into operation, reach specified high-speed stirred and shear, the vacuum control unit of simultaneously changing powder device starts to start, and the vacuum in making powder device is in-0.05MPa left and right fluctuation.After the stable operation of shear agitation device and vacuum balance and stability in changing powder device, milk powder inlet valve starts to open, under milk powder intake system is controlled, suction milk powder at regular time and quantity, the milk powder being inhaled into circulates after high speed shear stirs thawing between change milk container and change powder device.After milk powder in milk powder storehouse has all absorbed, milk powder suction valve closure.Now keep the constant and high speed shear of vacuum to stir operation, pigment mixed liquor is being changed milk container and is changing between powder device and continue circular flow.After reaching the circulation timei of technological requirement, vacuum-control(led) system and feed pump and inlet valve are out of service, and discharging pump, outlet valve and shear agitation device continue operation, and like this, the liquid level of changing in powder device reduces gradually.Finally the milk in changing powder tank is all after entering milk container, and discharging pump, outlet valve and shear agitation device are out of service, and pigment mixed process completes.
Claims (6)
1. a water-powder mixer, it is characterized in that, comprising milk container (1), change powder device (3), milk powder storehouse (5) and controller, in described change powder device (3), be provided with LOAD CELLS, shear agitation device and vacuum control unit, between described change milk container (1) and change powder device (3), be provided with feeding-passage and tapping channel, described feeding-passage is provided with feed pump (9) and inlet valve (4), described tapping channel is provided with discharging pump (8) and outlet valve (2), between described milk powder storehouse (5) and change powder device (3), be provided with suction passage, described suction passage is provided with milk powder inlet valve (6), described inlet valve (4), outlet valve (2) is connected with controller respectively with milk powder inlet valve (6).
2. water-powder mixer according to claim 1, is characterized in that, stirring clipper and cooling system that described shear agitation device comprises stirring motor, by stirring motor, driven.
3. water-powder mixer according to claim 1, it is characterized in that, described vacuum-control(led) system comprises vacuum sensor, vacuum transducer, vacuum governor, vavuum pump and the vacuum conditions magnetic valve being connected with vavuum pump, described vacuum sensor is connected with vacuum transducer, and described vacuum transducer, vacuum conditions magnetic valve are connected with vacuum governor respectively.
4. according to the water-powder mixer described in claim 1 or 2 or 3, it is characterized in that, between described outlet valve (2) and change powder device (3), be provided with circulation branch road, circulation branch road is provided with circulating valve (7).
5. according to the water-powder mixer described in claim 1 or 2 or 3, it is characterized in that, in described milk powder storehouse, be provided with powder position detecting sensor and silo-wall shaker, described powder position detecting sensor is connected respectively at controller with silo-wall shaker.
6. according to the water-powder mixer described in claim 1 or 2 or 3, it is characterized in that, described milk powder inlet valve (6) is connected with inhales powder delay controller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320415342.0U CN203417608U (en) | 2013-07-12 | 2013-07-12 | Liquid powder mixing machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320415342.0U CN203417608U (en) | 2013-07-12 | 2013-07-12 | Liquid powder mixing machine |
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| Publication Number | Publication Date |
|---|---|
| CN203417608U true CN203417608U (en) | 2014-02-05 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320415342.0U Expired - Fee Related CN203417608U (en) | 2013-07-12 | 2013-07-12 | Liquid powder mixing machine |
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| CN (1) | CN203417608U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108295754A (en) * | 2018-02-26 | 2018-07-20 | 福州法莫优科机械科技有限公司 | The filling integrated apparatus of emulsifying and its application method |
| CN109647270A (en) * | 2019-01-23 | 2019-04-19 | 江西蒙山乳业有限公司 | A kind of continuous circulation material system |
| CN112387150A (en) * | 2020-09-23 | 2021-02-23 | 海阳科技(江苏)研究院有限公司 | Preparation device and process of nano-scale carbon black suspension |
| CN112871043A (en) * | 2019-11-29 | 2021-06-01 | 内蒙古伊利实业集团股份有限公司 | Vacuum circulating material dissolving system and method for dairy product ingredients |
-
2013
- 2013-07-12 CN CN201320415342.0U patent/CN203417608U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108295754A (en) * | 2018-02-26 | 2018-07-20 | 福州法莫优科机械科技有限公司 | The filling integrated apparatus of emulsifying and its application method |
| CN109647270A (en) * | 2019-01-23 | 2019-04-19 | 江西蒙山乳业有限公司 | A kind of continuous circulation material system |
| CN112871043A (en) * | 2019-11-29 | 2021-06-01 | 内蒙古伊利实业集团股份有限公司 | Vacuum circulating material dissolving system and method for dairy product ingredients |
| CN112387150A (en) * | 2020-09-23 | 2021-02-23 | 海阳科技(江苏)研究院有限公司 | Preparation device and process of nano-scale carbon black suspension |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140205 Termination date: 20180712 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |