CN203663489U - Unit combined distillation and extraction device - Google Patents
Unit combined distillation and extraction device Download PDFInfo
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- CN203663489U CN203663489U CN201420037812.9U CN201420037812U CN203663489U CN 203663489 U CN203663489 U CN 203663489U CN 201420037812 U CN201420037812 U CN 201420037812U CN 203663489 U CN203663489 U CN 203663489U
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- extracting device
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- dividing plate
- steamer body
- combination type
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Abstract
The utility model relates to a unit combined distillation and extraction device which comprises a steamer body, a bottom steamer and a steamer cover. The steamer body is fixedly connected with the bottom steamer, a screen plate is fixedly arranged at the connecting position of the steamer body and the bottom steamer, holes are evenly formed in the surface of the screen plate, and the steamer cover is matched with the steamer body. A lower-layer partition plate and an upper-layer partition plate are evenly, parallelly and fixedly arranged in the steamer body, the lower-layer partition plate is located under the upper-layer partition plate, and the lower-layer partition plate and the upper-layer partition plate are distributed staggered. A sealing groove is arranged around the outer side of the upper end of the steamer body. Steam spraying pipes and heating pipes are arranged in the bottom steamer, and the steam spraying pipes are located above the heating pipes and parallelly arranged in heating units. A first sealing part is arranged around the outer side of the lower end of the steamer cover and movably embedded with the sealing groove. The steamer body and the bottom steamer are divided into heating units, so that steam flows are evenly distributed, the lower-layer partition plate and the upper-layer partition plate are arranged in a staggered mode, the steam and materials are in full contact, and the efficiency is high.
Description
Technical field
The utility model relates to a kind of unit-combination type distilling and extracting device, belongs to food and drink production equipment technical field.
Background technology
Solid-liquid mixed material distillation extraction equipment is a kind of solid feed is carried out to Steam Heating provide physics, the device of chemistry or biological respinse distillation extraction active ingredient.Temperature Distribution and moisture distribution to the material in container when material distillation extraction all have higher requirements, and the air-flow distribution good design tissue of reply equipment, guarantees the material uniformly transfer heat mass transfer in container, fully reaction.Normal food distillation extraction equipment adopts barrel shape structure, and device interior does not have air current composition to cut apart, and equipment size is little, and the thermal efficiency and production efficiency are low.
In existing distilling and extracting device, all distillation extraction space is not divided into multiple extraction cells, causes distillation extraction distribution of steam inequality, and the direction of steam flow does not fluctuate, and to cause Zheng to heat up in a steamer extraction efficiency low.
Summary of the invention
For the deficiencies in the prior art, the utility model provides a kind of unit-combination type distilling and extracting device.
The technical solution of the utility model is as follows:
A kind of unit-combination type distilling and extracting device, comprise steamer body, end pot and pot cover, described steamer body is fixedly connected with end pot, described steamer body and the junction of end pot are fixedly installed sieve plate, described sieve plate surface uniform arranges porose, described pot cover and matches with described steamer body;
Even parallel lower floor's dividing plate and the upper strata dividing plate of being fixedly installed in described steamer body, described lower floor's dividing plate is positioned at the below of described upper strata dividing plate, and described lower floor's dividing plate and described upper strata dividing plate are staggered; The bottom of described lower floor's dividing plate extend in end pot and and the bottom of end pot between be provided with space, described steamer body and described end pot are divided into heating unit by described lower floor's dividing plate and described upper strata dividing plate, and the upper end outer periphery of described steamer body is provided with seal groove;
In described end pot, be provided with steam jet pipe and heating tube, described steam jet pipe is arranged in the top of heating tube and is set in parallel in heating unit;
The lower end outer periphery of described pot cover is provided with the first seal chimeric with seal groove activity.
According to the utility model, preferred, described end pot is also provided with filling pipe and liquid level display.
According to the utility model, preferably, described pot cover is fixedly connected with blast pipe, and described blast pipe is communicated with described pot cover, on described blast pipe, be provided with air bleeding valve, on described blast pipe and between described air bleeding valve and described pot cover, be provided with Pressure gauge.
According to the utility model, preferably, described unit-combination type distilling and extracting device is also provided with lift rotary column, hydraulic mandril and the second seal, the second described seal is sliding sealing device and is movably arranged on blast pipe, described lift rotary column is connected with described blast pipe, and described hydraulic mandril is arranged on described lift rotary column.
According to the utility model, preferred, described unit-combination type distilling and extracting device is also provided with worm gear, worm-wheel shaft, worm screw and support bar; Described worm-wheel shaft is fixedly installed on steamer body, described worm gear is fixedly connected with described worm-wheel shaft, described worm screw and described worm wheel, the number of described support bar is 2 and is connected with worm-wheel shaft vertical support, and the worm-wheel shaft described in the height > of described support bar is to the height of described distilling and extracting device bottom.
According to the utility model, preferred, the number of described lower floor's dividing plate is 3～9, and the number of described upper strata dividing plate is 3～8.
According to the utility model, preferably, described steamer body is rectangular structure, and described end pot is the structure of falling truncated rectangular pyramids, the height of described end pot is 1/5～1/3 of described steamer body height, and the floor space of described end pot is 80～90% of described steamer body cross-section.
According to the utility model, preferred, the density of described sieve plate surface holes is 4～6/cm
2, the diameter in hole is 1.5～2mm.
According to the utility model, preferred, the part that described sieve plate is positioned at heating unit is convex configuration.
According to the utility model, preferred, the degree of depth of described seal groove is 5～10cm.
Unit-combination type distilling and extracting device described in the utility model can be applicable to the distillation extraction processing of food and wine brewing field raw material, is applied to the distillation extraction processing better processing effect of liquor-making raw material.
The beneficial effects of the utility model:
1, the utility model is owing to being provided with lower floor's dividing plate and upper strata dividing plate, steamer body and end pot are divided into heating unit, make the distribution of vapor stream more even, and lower floor's dividing plate and upper strata dividing plate staggered, distillation extraction steam contacts more abundant with material, distillation extraction efficiency is higher.
2, the utility model is owing to distilling and extracting device being divided into steamer body and end pot two parts, and residual water provides steam to material stifling preheating, the on the other hand vapour pressure in equlibrium distillation extraction equipment on the one hand; Heat by residual water and uperize two parts simultaneously, make the operation stable and uniform more of distilling and extracting device, each heating unit is by Di Guo UNICOM and by residual water position Dynamic Closed, when heating unit internal pressure changes, the vapor volume of residual water position and heating unit also changes thereupon, and then automatic fine has regulated the steam flow in each heating unit.
3, the utility model is owing to being provided with filling pipe and liquid level display at end pot, and when liquid level display shows that residual water drops to a certain degree, filling pipe supplements timely adjustment to residual water.
4, the utility model is owing to being provided with air bleeding valve and Pressure gauge on blast pipe, the pressure in the real-time detection display distilling and extracting device of Pressure gauge, according to circumstances by air bleeding valve to the pressure timely adjustment in distilling and extracting device.
5, the utility model, owing to being provided with lift rotary column and hydraulic mandril, having been realized pot cover and has been opened and closed automatic control, saves manpower, has improved production efficiency.
6, the utility model, owing to being provided with worm gear, worm-wheel shaft, worm screw and support bar, has been realized the automatic control of distilling and extracting device discharging.
7, the whole sieve plate of the utility model is concavo-convex alternate formula structure, and the part that sieve plate is positioned at heating unit is convex configuration, makes on airflow direction, to have reduced the attached wall phenomenon of retort gas in distilling and extracting device.
8, the utility model is owing to being provided with seal groove and the first seal, and steam-condensation becomes liquid water to be filled in seal groove, forms tank sealing, has fully guaranteed the sealing in steaming plant.
Accompanying drawing explanation
Fig. 1 is the agent structure schematic diagram of unit-combination type distilling and extracting device in the utility model embodiment 1.
Fig. 2 is the cutaway view of unit-combination type distilling and extracting device A-A direction in the utility model embodiment 1.
Fig. 3 is the agent structure schematic diagram of unit-combination type distilling and extracting device in the utility model embodiment 2.
Fig. 4 is the agent structure schematic diagram of unit-combination type distilling and extracting device in the utility model embodiment 4.
Fig. 5 is the agent structure schematic diagram of unit-combination type distilling and extracting device in the utility model embodiment 5.
In figure: 1, steamer body, 2, end pot, 3, pot cover, 4, sieve plate, 5, lower floor's dividing plate, 6, upper strata dividing plate, 7, steam jet pipe, 8, heating tube, 9, the first seal, 10, seal groove, 11, filling pipe, 12, liquid level display, 13, blast pipe, 14, lift rotary column, 15, hydraulic mandril, 16, the second seal, 17, air bleeding valve, 18, Pressure gauge, 19, worm gear, 20, worm-wheel shaft, 21, worm screw, 22, support bar.
The specific embodiment
Below by specific embodiment, the utility model is described further, but is not limited to this.
A kind of unit-combination type distilling and extracting device, comprise steamer body 1, end pot 2 and pot cover 3, described steamer body 1 is fixedly connected with end pot 2, described steamer body 1 and the junction of end pot 2 are fixedly installed sieve plate 4, described sieve plate 4 surface uniforms arrange porose, described pot cover 3 and match with described steamer body 1;
Even parallel lower floor's dividing plate 5 and the upper strata dividing plate 6 of being fixedly installed in described steamer body 1, described lower floor's dividing plate 5 is positioned at the below of described upper strata dividing plate 6, and described lower floor's dividing plate 5 is staggered with described upper strata dividing plate 6; The bottom of described lower floor's dividing plate 5 extend in end pot 2 and and the bottom of end pot 2 between be provided with space, described steamer body 1 and described end pot 2 are divided into heating unit by described lower floor's dividing plate 5 and described upper strata dividing plate 6, and the upper end outer periphery of described steamer body 1 is provided with seal groove 10;
In described end pot 2, be provided with steam jet pipe 7 and heating tube 8, described steam jet pipe 7 is arranged in the top of heating tube 8 and is set in parallel in heating unit;
The lower end outer periphery of described pot cover 3 is provided with the first seal 9 movable chimeric with seal groove 10.
In the present embodiment, described steamer body 1 is rectangular structure, and described end pot 2 is the structure of falling truncated rectangular pyramids, the height of described end pot 2 be described steamer body 1 highly 1/4, the floor space of described end pot 2 is 80% of described steamer body 1 cross section; The number of described lower floor's dividing plate 5 is 9, and the number of described upper strata dividing plate 6 is 8, that is, the bottom of steamer body 1 and end pot 2 are divided into 10 heating units by lower floor's dividing plate 5, and the top of steamer body 1 is divided into 9 heating units by upper strata dividing plate 6; The density of described sieve plate 4 surface holes is 4～6/cm2, and the diameter in hole is 1.5～2mm, and the part that sieve plate 4 is positioned at heating unit is convex configuration; The degree of depth of described seal groove 6 is 5～10cm.
When unit-combination type distilling and extracting device uses in the present embodiment, open pot cover 3, add residual water, the material of extraction to be distilled is joined in distilling and extracting device, cover pot cover 3; Heating tube 8 is fumigated after the preheated one-section time material residual water heating generation steam, and steam jet pipe 7 uperizes are to material high temperature distillation extraction, the Temperature Distribution in the steam supply control distilling and extracting device of adjustable steam jet pipe 7.
Owing to being provided with lower floor's dividing plate 5 and upper strata dividing plate 6, steamer body 1 and end pot 2 are divided into heating unit, make the distribution of vapor stream more even, and lower floor's dividing plate 5 and upper strata dividing plate 6 staggered, distillation extraction steam contacts more abundant with material, distillation extraction efficiency is higher; Because whole sieve plate 4 is concavo-convex alternate formula structure, the part that sieve plate 4 is positioned at heating unit is convex configuration, makes on airflow direction, to have reduced the attached wall phenomenon of boiling gas in distilling and extracting device; Distilling and extracting device is divided into steamer body 1 and end pot 2 two parts, and residual water provides steam to material stifling preheating, the on the other hand vapour pressure in equlibrium distillation extraction equipment on the one hand; Heat by residual water and uperize two parts simultaneously, make the operation stable and uniform more of distilling and extracting device, each heating unit is by Di Guo 2 UNICOMs and by residual water position Dynamic Closed, when heating unit internal pressure changes, the vapor volume of residual water position and heating unit also changes thereupon, and then automatic fine has regulated the steam flow in each heating unit; Owing to being provided with seal groove 10 and the first seal 9, steam-condensation becomes liquid water to be filled in seal groove 10, forms tank sealing, has fully guaranteed the sealing in distilling and extracting device.
Unit-combination type distilling and extracting device as described in Example 1, different is that described end pot 2 is also provided with filling pipe 11 and liquid level display 12.
Described filling pipe 11 is for supplementing residual water, and described liquid level display 12 is for showing the water level of residual water.When residual water position drops to a certain degree, filling pipe 11 will supplement residual water in time.
In the present embodiment, the number of described lower floor's dividing plate 5 is 6, and the number of described upper strata dividing plate 6 is 5.
Embodiment 3
Unit-combination type distilling and extracting device as described in Example 2, different is that described pot cover 3 is fixedly connected with blast pipe 13, described blast pipe 13 is communicated with described pot cover 3, on described blast pipe 13, be provided with air bleeding valve 17, on described blast pipe 13 and between described air bleeding valve 17 and described pot cover 3, be provided with Pressure gauge 18.
Described air bleeding valve 17 is for the pressure in timely adjustment distilling and extracting device, and described Pressure gauge 18 is for measuring the pressure showing in distilling and extracting device.
In the present embodiment, the number of described lower floor's dividing plate 5 is 3, and the number of described upper strata dividing plate 6 is 3.
Unit-combination type distilling and extracting device as described in Example 3, different is that described unit-combination type distilling and extracting device is also provided with lift rotary column 14, hydraulic mandril 15 and the second seal 16, the second described seal 16 is sliding sealing device and is movably arranged on blast pipe 13, described lift rotary column 14 is connected with described blast pipe 13, and described hydraulic mandril 15 is arranged on described lift rotary column 14.
In the present embodiment, the number of described lower floor's dividing plate 5 is 4, and the number of described upper strata dividing plate 6 is 3.On blast pipe 13, be provided with the second seal 16, realize the sealing of blast pipe 13 by slipper seal, the existing device of realizing slipper seal all can be used as the second seal 16.While opening pot cover 3, by the jacking of hydraulic mandril 15, blast pipe 13 is promoted to certain altitude together with pot cover 3, by the rotation of lift rotary column 14, pot cover 3 is moved out; When closed pot cover 3,, and then realize pot cover 3 and opened and closed automatic control pot cover 3 closures by the rotation of lift rotary column 14 and the landing of hydraulic mandril 15, saved manpower, improved production efficiency.
Unit-combination type distilling and extracting device as described in Example 4, different is that described unit-combination type distilling and extracting device is also provided with worm gear 19, worm-wheel shaft 20, worm screw 21 and support bar 22; Described worm-wheel shaft 20 is fixedly installed on steamer body 1, described worm gear 19 is fixedly connected with described worm-wheel shaft 20, described worm screw 21 is matched with described worm gear 19, the number of described support bar 22 is 2 and is connected with worm-wheel shaft 20 vertical support, and the worm-wheel shaft 20 described in the height > of described support bar 22 is to the height of described distilling and extracting device bottom.
In the present embodiment, the number of described lower floor's dividing plate 5 is 7, and the number of described upper strata dividing plate 6 is 6.Because the worm-wheel shaft 20 described in the height > of described support bar 22 is to the height of described distilling and extracting device bottom, distilling and extracting device is supported built on stilts by described support bar 22, rotary worm 21 drives worm gear 19 to rotate, and then realize the rotation of distilling and extracting device, finally realize the automatic control of distilling and extracting device discharging.
Claims (10)
1. a unit-combination type distilling and extracting device, it is characterized in that, this distilling and extracting device comprises steamer body, end pot and pot cover, described steamer body is fixedly connected with end pot, described steamer body and the junction of end pot are fixedly installed sieve plate, described sieve plate surface uniform arranges porose, described pot cover and matches with described steamer body;
Even parallel lower floor's dividing plate and the upper strata dividing plate of being fixedly installed in described steamer body, described lower floor's dividing plate is positioned at the below of described upper strata dividing plate, and described lower floor's dividing plate and described upper strata dividing plate are staggered; The bottom of described lower floor's dividing plate extend in end pot and and the bottom of end pot between be provided with space, described steamer body and described end pot are divided into heating unit by described lower floor's dividing plate and described upper strata dividing plate, and the upper end outer periphery of described steamer body is provided with seal groove;
In described end pot, be provided with steam jet pipe and heating tube, described steam jet pipe is arranged in the top of heating tube and is set in parallel in heating unit;
The lower end outer periphery of described pot cover is provided with the first seal chimeric with seal groove activity.
2. unit-combination type distilling and extracting device according to claim 1, is characterized in that, described end pot is also provided with filling pipe and liquid level display.
3. unit-combination type distilling and extracting device according to claim 2, it is characterized in that, described pot cover is fixedly connected with blast pipe, described blast pipe is communicated with described pot cover, on described blast pipe, be provided with air bleeding valve, on described blast pipe and between described air bleeding valve and described pot cover, be provided with Pressure gauge.
4. unit-combination type distilling and extracting device according to claim 3, it is characterized in that, described unit-combination type distilling and extracting device is also provided with lift rotary column, hydraulic mandril and the second seal, the second described seal is sliding sealing device and is movably arranged on blast pipe, described lift rotary column is connected with described blast pipe, and described hydraulic mandril is arranged on described lift rotary column.
5. unit-combination type distilling and extracting device according to claim 4, is characterized in that, described unit-combination type distilling and extracting device is also provided with worm gear, worm-wheel shaft, worm screw and support bar; Described worm-wheel shaft is fixedly installed on steamer body, described worm gear is fixedly connected with described worm-wheel shaft, described worm screw and described worm wheel, the number of described support bar is 2 and is connected with worm-wheel shaft vertical support, and the worm-wheel shaft described in the height > of described support bar is to the height of described distilling and extracting device bottom.
6. according to the unit-combination type distilling and extracting device described in claim 1～5 any one, it is characterized in that, the number of described lower floor's dividing plate is 3～9, and the number of described upper strata dividing plate is 3～8.
7. according to the unit-combination type distilling and extracting device described in claim 1～5 any one, it is characterized in that, described steamer body is rectangular structure, described end pot is the structure of falling truncated rectangular pyramids, the height of described end pot is 1/5～1/3 of described steamer body height, and the floor space of described end pot is 80～90% of described steamer body cross-section.
8. according to the unit-combination type distilling and extracting device described in claim 1～5 any one, it is characterized in that, the density of described sieve plate surface holes is 4～6/cm
2, the diameter in hole is 1.5～2mm.
9. according to the unit-combination type distilling and extracting device described in claim 1～5 any one, it is characterized in that, the part that described sieve plate is positioned at heating unit is convex configuration.
10. according to the unit-combination type distilling and extracting device described in claim 1～5 any one, it is characterized in that, the degree of depth of described seal groove is 5～10cm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420037812.9U CN203663489U (en) | 2014-01-21 | 2014-01-21 | Unit combined distillation and extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420037812.9U CN203663489U (en) | 2014-01-21 | 2014-01-21 | Unit combined distillation and extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203663489U true CN203663489U (en) | 2014-06-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420037812.9U Withdrawn - After Issue CN203663489U (en) | 2014-01-21 | 2014-01-21 | Unit combined distillation and extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203663489U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103736291A (en) * | 2014-01-21 | 2014-04-23 | 山东省轻工业设计院 | Unit combination type distillation and extraction device |
-
2014
- 2014-01-21 CN CN201420037812.9U patent/CN203663489U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103736291A (en) * | 2014-01-21 | 2014-04-23 | 山东省轻工业设计院 | Unit combination type distillation and extraction device |
| CN103736291B (en) * | 2014-01-21 | 2016-02-24 | 山东省轻工业设计院 | A kind of unit-combination type distilling and extracting device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20140625 Effective date of abandoning: 20160224 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |