CN210560321U - Essence recovery unit in tuber class raw whole flour production process - Google Patents
Essence recovery unit in tuber class raw whole flour production process Download PDFInfo
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- CN210560321U CN210560321U CN201921120264.5U CN201921120264U CN210560321U CN 210560321 U CN210560321 U CN 210560321U CN 201921120264 U CN201921120264 U CN 201921120264U CN 210560321 U CN210560321 U CN 210560321U
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- 238000011084 recovery Methods 0.000 title claims abstract description 22
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 17
- 235000013312 flour Nutrition 0.000 title claims description 15
- 238000009833 condensation Methods 0.000 claims abstract description 61
- 230000005494 condensation Effects 0.000 claims abstract description 61
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 44
- 238000001816 cooling Methods 0.000 claims abstract description 41
- 239000007921 spray Substances 0.000 claims abstract description 36
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 238000005507 spraying Methods 0.000 claims abstract description 19
- 238000001514 detection method Methods 0.000 claims description 3
- 238000004321 preservation Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 6
- 238000009434 installation Methods 0.000 abstract description 5
- 239000000843 powder Substances 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 abstract 1
- 241001233242 Lontra Species 0.000 description 3
- 235000013311 vegetables Nutrition 0.000 description 3
- 235000002595 Solanum tuberosum Nutrition 0.000 description 2
- 244000061456 Solanum tuberosum Species 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000012015 potatoes Nutrition 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 235000000832 Ayote Nutrition 0.000 description 1
- 235000006481 Colocasia esculenta Nutrition 0.000 description 1
- 244000205754 Colocasia esculenta Species 0.000 description 1
- 241000219122 Cucurbita Species 0.000 description 1
- 235000009854 Cucurbita moschata Nutrition 0.000 description 1
- 235000009804 Cucurbita pepo subsp pepo Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 235000004879 dioscorea Nutrition 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000015136 pumpkin Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model provides an essence recovery unit in crude full powder production process of tuber class, belongs to tuber class processing technology field, and it includes: the device comprises a bin body, a cooling pipe, an air inlet mechanism, a condensing mechanism and a spraying mechanism; the bin body comprises a condensation section and a cooling section; the cooling section is connected to the lower end of the condensing section, a liquid outlet pipe is arranged at the bottom of the cooling section, and a main switch is arranged at the liquid outlet pipe; the top of the bin body is provided with an air outlet; the cooling pipe disc is arranged in the cooling section, a water inlet and a water outlet of the cooling pipe extend out of the cooling section, and the water inlet is lower than the water outlet; the air inlet mechanism comprises an air inlet pipe and a plurality of air distribution pipes; the condensation mechanism comprises a plurality of installation screen plates and a plurality of condensation pipes; the spraying mechanism arranged at the upper end of the condensation section comprises a spraying pipe, a spray head and a spraying pump. Simple structure, the simple operation can be retrieved with the steam rapid condensation who has tuber class material essence, and the condensation is effectual, and recovery efficiency is high.
Description
Technical Field
The utility model belongs to the technical field of tuber class processing technique and specifically relates to an essence recovery unit in tuber class raw flour production process is related to.
Background
Common tuber vegetables comprise potatoes, yams, potatoes, pumpkins, taros and the like, and when the tuber vegetables are processed, the tuber vegetables need to be cleaned, diced, dried, crushed, packaged and other procedures; in the drying procedure, the dried steam has no harmful substances and is often directly discharged outside, the steam contains essence of tuber materials, the essence is widely applied in the fields of cooking, baking and the like, if the essence is directly discharged outside, waste is caused, and meanwhile, certain pollution is caused to air.
Therefore, it is necessary to design an essence recycling device in the production process of tuber raw whole flour to solve the above problems.
SUMMERY OF THE UTILITY MODEL
In order to avoid above-mentioned problem, provide an essence recovery unit in tuber class raw full powder production process, simple structure, the simple operation can be retrieved with the steam rapid condensation who has tuber class material essence, and the condensation is effectual, and recovery efficiency is high.
The utility model provides a pair of essence recovery unit in tuber class raw whole flour production process, include: the device comprises a bin body, a cooling pipe, an air inlet mechanism, a condensing mechanism and a spraying mechanism;
the bin body comprises a condensation section and a cooling section; the cooling section is connected to the lower end of the condensing section, a liquid outlet pipe is arranged at the bottom of the cooling section, and a main switch is arranged at the liquid outlet pipe; the top of the bin body is provided with an air outlet;
the cooling pipe disc is arranged in the cooling section, a water inlet and a water outlet of the cooling pipe extend out of the cooling section, and the water inlet is lower than the water outlet;
the air inlet mechanism comprises an air inlet pipe and a plurality of air distribution pipes, the air inlet pipe extends into the lower end of the condensation section, one end of the air inlet pipe, which is positioned in the condensation section, is respectively connected with the plurality of air distribution pipes, each air distribution pipe is provided with a plurality of air outlet holes in the direction, and each air distribution pipe is provided with at least one outlet downwards;
the condensation mechanism comprises a plurality of mounting net plates and a plurality of condensation pipes, the mounting net plates are sequentially mounted in the middle of the condensation section from bottom to top, the condensation pipes are correspondingly coiled on the mounting net plates one by one, and the water inlet end of each condensation pipe is lower than the water outlet end; the water inlet end of the middle condensing pipe is connected with the water outlet end of the adjacent lower layer condensing pipe, and the water outlet end of the middle condensing pipe is connected with the water inlet end of the adjacent upper layer condensing pipe; the water inlet end of the lowest layer of condensing pipe and the water outlet end of the uppermost layer of condensing pipe extend out of the condensing section;
the spraying mechanism comprises a spraying pipe, a spray head and a spraying pump; one end of the spray pipe extends into the upper end of the condensation section, the spray head is arranged at one end of the spray pipe, which is positioned inside the condensation section, and the spray pump is connected with the spray pipe and sends the liquid coming out of the liquid outlet pipe to the spray head through the spray pipe.
Preferably, the spray head is rotatably mounted at one end of the spray pipe positioned in the condensation section.
Preferably, the gas distribution pipe is arc-shaped.
Preferably, the outside of the bin body is provided with an insulating layer.
Preferably, the liquid outlet pipe and the upper end and the lower end of the condensation section are both connected with the temperature detection device.
Preferably, the liquid outlet pipe is connected with at least two liquid outlet branch pipes, and each liquid outlet branch pipe is provided with a branch switch.
Preferably, a fan is provided at the air outlet.
Preferably, the upper end of the condensation section is provided with a gas baffle, and the gas baffle is provided with a plurality of gas outlet through holes and is positioned above the spraying mechanism.
Compared with the prior art, the utility model discloses following beneficial effect has: simple structure, the simple operation can be retrieved with the steam rapid condensation who has tuber class material essence, and the condensation is effectual, and recovery efficiency is high.
Drawings
Fig. 1 is a schematic structural view of an essence recycling device in the production process of tuber raw whole flour according to a preferred embodiment of the present invention;
detailed description of the embodiments reference is made to the accompanying drawings in which:
1. a bin body 11, a condensing section 12, a cooling section 13, a liquid outlet pipe 14, a main switch 15, an air outlet 16, a liquid outlet branch pipe 17, a branch switch 18 and a fan,
2. a cooling pipe 21, a water inlet 22 and a water outlet,
3. an air inlet mechanism 31, an air inlet pipe 32, a gas distribution pipe 33, an air outlet hole 34 and an outlet,
4. a condensing mechanism 41, an installation screen plate 42, a condensing pipe 43, a water inlet end 44 and a water outlet end,
5. a spraying mechanism 51, a spraying pipe 52 and a spray head,
6. an insulating layer is arranged on the inner wall of the heat-insulating layer,
7. a gas baffle plate.
Detailed Description
The technical solution of the present invention will be clearly and completely described with reference to the accompanying drawings. In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", and the like indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplification of description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art.
As shown in fig. 1, the essence recovery device in the production process of tuber raw whole flour provided by this embodiment includes: the device comprises a bin body 1, a cooling pipe 2, an air inlet mechanism 3, a condensing mechanism 4 and a spraying mechanism 5.
As shown in fig. 1, the bin body 1 comprises a condensation section 11 and a cooling section 12; the cooling section 12 is connected to the lower end of the condensing section 11, a liquid outlet pipe 13 is arranged at the bottom of the cooling section 12, and a main switch 14 is arranged at the liquid outlet pipe 13; the top of the bin body 1 is provided with an air outlet 15. The gas is condensed into liquid in the condensing section 11 and falls into the cooling section 12; simultaneously, 2 coils of cooling tube are established inside cooling zone 12, and cooling zone 12 is all stretched out to the water inlet 21 and the delivery port 22 of cooling tube 2, and water inlet 21 is less than delivery port 22, and the cold water that water inlet 21 entered can be to liquid cooling down in the cooling zone 12, and refrigerated temperature can be decided according to the demand, and is practical high-efficient, can ensure simultaneously that follow-up temperature when providing the spray liquid for spraying mechanism 5 is lower, reaches ideal effect.
As shown in fig. 1, the air intake mechanism 3 includes an air intake pipe 31 and a plurality of air distribution pipes 32, the air intake pipe 31 extends into the lower end of the condensation section 11, one end of the air intake pipe 31 located in the condensation section 11 is respectively connected with the plurality of air distribution pipes 32, each air distribution pipe 32 is provided with a plurality of air outlet holes 33 facing downward, and each air distribution pipe 32 is provided with at least one outlet 34 facing downward; the gas is respectively fed through the plurality of gas distributing pipes 32, the gas required to be condensed can be dispersed and discharged through the plurality of gas outlet holes 33, the subsequent condensation operation is facilitated, and the condensation efficiency can be greatly improved. In this embodiment, the gas distribution pipe 32 is arc-shaped, and the gas dispersion range is increased.
Meanwhile, the condensing mechanism 4 comprises a plurality of mounting net plates 41 and a plurality of condensing pipes 42, the mounting net plates 41 are sequentially mounted in the middle of the condensing section 11 from bottom to top, the condensing pipes 42 are correspondingly coiled on the mounting net plates 41 one by one, and the water inlet end 43 of each condensing pipe 42 is lower than the water outlet end 44; the water inlet end 43 of the middle condensing pipe 42 is connected with the water outlet end 44 of the condensing pipe 42 of the next adjacent layer, and the water outlet end 44 of the middle condensing pipe 42 is connected with the water inlet end 43 of the condensing pipe 42 of the previous adjacent layer; the water inlet end 43 of the lowest condensation pipe 42 and the water outlet end 44 of the highest condensation pipe 42 extend out of the condensation section 11. The dish that condenser pipe 42 is M form is established on installation otter board 41, can directly carry out the condensation to gas, can condense installation otter board 41 simultaneously again, and installation otter board 41 has also had the condensation to gas like this simultaneously, and the condensation is effectual, improves condensation efficiency.
As shown in fig. 1, the spray mechanism 5 includes a spray pipe 51, a spray head 52, and a spray pump. One end of the spray pipe 51 extends into the upper end of the condensation section 11, the spray head 52 is arranged at one end of the spray pipe 51 positioned in the condensation section 11, the spray pump is connected with the spray pipe 51 and sends the liquid from the liquid outlet pipe 13 to the spray head 52 through the spray pipe 51; liquid circulation after the condensation cooling condenses gas, avoids in the gas adulterated other thing, can be to the high-efficient condensation of gas again. Meanwhile, the spray head 52 is rotatably installed at one end of the spray pipe 51 inside the condensation section 11, so that the spray range and the contact area with the gas can be greatly increased.
Further, be equipped with gas baffle 7 in condensation section 11 upper end, be equipped with a plurality of outlet vent holes on gas baffle 7 and be located spray mechanism 5 top, can do last condensation to gas and block, improve the rate of recovery. And the heat preservation layer 6 is arranged outside the bin body 1, so that the energy loss during cooling and condensation is avoided, and the recovery efficiency is improved.
Furthermore, the upper end and the lower end of the liquid outlet pipe 13 and the upper end and the lower end of the condensation section 11 are both connected with a temperature detection device, so that the temperature of each section can be detected, and the control and the adjustment are convenient.
As shown in fig. 1, the liquid outlet pipe 13 is connected with at least two liquid outlet branch pipes 16, and each liquid outlet branch pipe 16 is provided with a branch switch 17; the liquid receiving device is convenient to replace. And, a fan 18 is provided at the air outlet 15.
When the device is used, steam containing tuber material essence to be condensed and recovered enters the condensation section 11 through the air inlet mechanism 3, is condensed through the condensation mechanism 4 and the spraying mechanism 5, is condensed into liquid, falls into the cooling section 12, is cooled through the cooling pipe 2, and then is discharged through the liquid outlet pipe 13; the other uncondensed components continue to move upward and exit through the gas outlet 15.
This recovery unit simple structure, the simple operation can be retrieved with the steam rapid condensation who has tuber class material essence, and the condensation is effectual, and recovery efficiency is high.
Novel solutions, not limitations thereof; although the present invention has been described in detail with reference to the foregoing embodiments, it should be understood by those skilled in the art that: the technical solutions described in the foregoing embodiments may still be modified, or some or all of the technical features may be equivalently replaced; such modifications and substitutions do not depart from the spirit and scope of the present invention.
Claims (8)
1. The utility model provides an essence recovery unit in tuber class raw flour production process which characterized in that includes: the device comprises a bin body, a cooling pipe, an air inlet mechanism, a condensing mechanism and a spraying mechanism;
the bin body comprises a condensation section and a cooling section; the cooling section is connected to the lower end of the condensing section, a liquid outlet pipe is arranged at the bottom of the cooling section, and a main switch is arranged at the liquid outlet pipe; the top of the bin body is provided with an air outlet;
the cooling pipe disc is arranged in the cooling section, a water inlet and a water outlet of the cooling pipe extend out of the cooling section, and the water inlet is lower than the water outlet;
the air inlet mechanism comprises an air inlet pipe and a plurality of air distribution pipes, the air inlet pipe extends into the lower end of the condensation section, one end of the air inlet pipe, which is positioned in the condensation section, is respectively connected with the plurality of air distribution pipes, each air distribution pipe is provided with a plurality of air outlet holes in the direction, and each air distribution pipe is provided with at least one outlet downwards;
the condensation mechanism comprises a plurality of mounting net plates and a plurality of condensation pipes, the mounting net plates are sequentially mounted in the middle of the condensation section from bottom to top, the condensation pipes are correspondingly coiled on the mounting net plates one by one, and the water inlet end of each condensation pipe is lower than the water outlet end; the water inlet end of the middle condensing pipe is connected with the water outlet end of the adjacent lower layer condensing pipe, and the water outlet end of the middle condensing pipe is connected with the water inlet end of the adjacent upper layer condensing pipe; the water inlet end of the lowest layer of condensing pipe and the water outlet end of the uppermost layer of condensing pipe extend out of the condensing section;
the spraying mechanism comprises a spraying pipe, a spray head and a spraying pump; one end of the spray pipe extends into the upper end of the condensation section, the spray head is arranged at one end of the spray pipe, which is positioned inside the condensation section, and the spray pump is connected with the spray pipe and sends the liquid coming out of the liquid outlet pipe to the spray head through the spray pipe.
2. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the shower nozzle rotates and installs the one end that is located the condensation segment inside at the shower.
3. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the shape of the gas distribution pipe is arc.
4. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the outside of the bin body is provided with a heat preservation layer.
5. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the upper end and the lower end of the liquid outlet pipe and the upper end and the lower end of the condensation section are both connected with a temperature detection device.
6. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the liquid outlet pipe is connected with at least two liquid outlet branch pipes, and each liquid outlet branch pipe is provided with a branch switch.
7. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: a fan is arranged at the air outlet.
8. The essence recovery device in the production process of the tuber raw whole flour as claimed in claim 1, characterized in that: the upper end of the condensation section is provided with a gas baffle, and the gas baffle is provided with a plurality of gas outlet through holes and is positioned above the spraying mechanism.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921120264.5U CN210560321U (en) | 2019-07-17 | 2019-07-17 | Essence recovery unit in tuber class raw whole flour production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921120264.5U CN210560321U (en) | 2019-07-17 | 2019-07-17 | Essence recovery unit in tuber class raw whole flour production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN210560321U true CN210560321U (en) | 2020-05-19 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921120264.5U Active CN210560321U (en) | 2019-07-17 | 2019-07-17 | Essence recovery unit in tuber class raw whole flour production process |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN210560321U (en) |
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2019
- 2019-07-17 CN CN201921120264.5U patent/CN210560321U/en active Active
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