CN216236914U - Continuous steam stripping device - Google Patents
Continuous steam stripping device Download PDFInfo
- Publication number
- CN216236914U CN216236914U CN202122674220.0U CN202122674220U CN216236914U CN 216236914 U CN216236914 U CN 216236914U CN 202122674220 U CN202122674220 U CN 202122674220U CN 216236914 U CN216236914 U CN 216236914U
- Authority
- CN
- China
- Prior art keywords
- feed liquid
- stripping tower
- stripping
- spraying system
- condenser
- 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.)
- Active
Links
Images
Landscapes
- Extraction Or Liquid Replacement (AREA)
Abstract
The utility model relates to a continuous stripping device, which belongs to the technical field of essence and spice extraction and comprises a stripping tower (1), a feed liquid tank (2), a feed liquid pump (3), a heater (4), a condenser (5) and a finished product tank (6); a feed liquid spraying system (7) is arranged in the middle of the stripping tower (1), a steam coil pipe (8) is arranged at the bottom of the stripping tower, and a demister is arranged at the top of the stripping tower; the feed liquid tank (2) is connected between the bottom of the stripping tower (1) and an inlet of the feed liquid pump (3); an outlet pipe of the feed liquid pump (3) is communicated to a feed liquid spraying system (7); the heater (4) is arranged between the feed liquid pump (3) and the feed liquid spraying system (7); the inlet of the condenser (5) is communicated with a gas phase pipeline at the top of the stripping tower (1); the finished product tank (6) is communicated with an outlet pipe of the condenser (5); the utility model can effectively improve the purity and yield of the product, reduce the production cost and improve the production efficiency.
Description
Technical Field
The utility model belongs to the technical field of essence and spice extraction, and particularly relates to a continuous stripping device.
Background
The plant is the essence spices extraction source commonly used, and present essence spices extraction technique draws the plant earlier, obtains the extract of composition complicacy, and in order to obtain the pure material of composition singleness, need further steam stripping, and present stripping equipment, extraction efficiency is low, and mostly is intermittent type formula production, once only adds the material in the extraction tank promptly, draws the completion after, carries out next extraction again, and this kind of extraction mode not only extraction efficiency is low, and the product yield is also lower.
Disclosure of Invention
In order to overcome the problems in the background art, the utility model provides a continuous stripping device which is simple to operate, can effectively improve the purity and yield of products, reduces the production cost and improves the production efficiency.
In order to realize the purpose, the utility model is realized by the following technical scheme:
the continuous stripping device comprises a stripping tower, a feed liquid tank, a feed liquid pump, a heater, a condenser and a finished product tank; the middle part of the stripping tower is provided with a feed liquid spraying system, the bottom of the stripping tower is provided with a steam coil pipe, and the top of the stripping tower is provided with a demister; the feed liquid tank is connected between the bottom of the stripping tower and the inlet of the feed liquid pump; an outlet pipe of the feed liquid pump is communicated to the feed liquid spraying system, and a heater is arranged between the feed liquid pump and the feed liquid spraying system; the inlet of the condenser is communicated with a gas phase pipeline at the top of the stripping tower; and the finished product tank is communicated with an outlet pipe of the condenser.
Preferably, the demister is a defoaming plate and is provided with two layers, the lower layer is a grid type defoaming plate, and the upper layer is an S-shaped defoaming plate.
Preferably, the stripping tower is provided with a throat pipe above the feed liquid spraying system; the demister is arranged above the throat pipe.
Preferably, the spray head of the feed liquid spraying system is a spiral spray head.
The utility model has the beneficial effects that:
according to the utility model, the steam pipe and the feed liquid spraying system are arranged in the stripping tower, the steam and the feed liquid are in countercurrent contact, the extraction efficiency is effectively improved, and the demister is arranged, so that liquid drops can be collected back to the feed liquid tank, and the product purity is improved; the lower square defoaming plate has the effects of further dispersing feed liquid and gas and enhancing contact, the upper S-shaped defoaming plate can effectively collect liquid drops, and the arrangement of the double-layer defoaming plate not only enhances extraction, but also can effectively collect liquid drops; by arranging the throat pipe and arranging the demister on the throat pipe, after the feed liquid and the steam are in countercurrent contact extraction, the flow velocity is suddenly changed when the feed liquid passes through the throat pipe, and the mixing effect is further enhanced; by arranging the spiral spray head, the material sprayed by the material liquid spraying system has better spraying effect, and the spraying liquid has a certain rotating track, so that the spraying liquid can swirl steam, and the contact effect of the steam and the material liquid is further enhanced;
the utility model can realize continuous circulation extraction of materials, and the liquid drops collected by the demister can be extracted circularly, thereby further improving the product yield.
Drawings
FIG. 1 is a schematic structural view of the present invention;
FIG. 2 is a cross-sectional view of the upper demister plate of the present invention;
FIG. 3 is a top view of the lower demister plate of the present invention;
in the figure, 1-stripping tower, 2-feed liquid tank, 3-feed liquid pump, 4-heater, 5-condenser, 6-product tank, 7-feed liquid spraying system, 8-steam coil, 9-upper defoaming plate, 10-lower defoaming plate and 11-throat pipe.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, preferred embodiments of the present invention will be described in detail below with reference to the accompanying drawings to facilitate understanding of the skilled person.
As shown in fig. 1 to 3, the continuous stripping apparatus includes a stripping column 1, a feed liquid tank 2, a feed liquid pump 3, a heater 4, a condenser 5 and a product tank 6.
The feed liquid tank 2 is connected between the bottom of the stripping tower 1 and the inlet of the feed liquid pump 3, the outlet pipe of the feed liquid pump 3 is communicated to the feed liquid spraying system 7, the heater 4 is arranged between the feed liquid pump 3 and the feed liquid spraying system 7, the inlet of the condenser 5 is communicated with the gas phase pipeline at the top of the stripping tower 1, and the finished product tank 6 is communicated with the outlet pipe of the condenser 5. The feed tank 2 is provided with a feed pipe and a discharge pipe to realize material balance in the stripping process through feeding and discharging. The feed liquid is conveyed into the heater 4 by the feed liquid pump 3 to be heated and then is conveyed into the stripping tower by the feed liquid spraying system 7, after the stripping is finished in the stripping tower 1, the target product enters the condenser 5 through a gas phase pipeline at the top of the stripping tower 1 and enters the finished product tank 6 after being condensed by the condenser 5.
The steam coil 8 is arranged at the bottom of the stripping tower 1, saturated steam is provided for the steam coil 8 through a steam pipeline, feed liquid is sprayed by the feed liquid spraying system 7 and is in countercurrent contact with the steam, the contact area of the atomized feed liquid and the steam is large, and the stripping efficiency is high. The spray head of the feed liquid spraying system 7 is a spiral spray head, and the feed liquid sprayed by the spiral spray head has a certain rotating track, so that the spiral spray head can generate a rotating action on steam, and the contact effect of the steam and the feed liquid is further enhanced. Through set up heater 4 on the 3 outlet pipes of feed liquid pump, adopt feed liquid and steam to strip against the current in the strip tower 1, so, can avoid feed liquid and steam difference in temperature too big, the gas temperature in the strip tower 1 is better controlled simultaneously.
The stripping tower 1 is provided with a throat 10 above the feed liquid spraying system 7, and the demister is arranged above the throat 10. The demister comprises an upper defoaming plate 11 and a lower defoaming plate 12, the upper defoaming plate 11 is an S-shaped defoaming plate, and the lower defoaming plate 12 is a grid-shaped defoaming plate. The lower floor removes the design of foam board 12 and is square, when collecting the liquid drop, further disperses, strengthens gaseous effect to the gaseous material, and upper strata removes foam board 11 design and is the S type, can effectively collect the liquid drop, and the setting of double-deck foam board is not only strengthened extracting, and can effectively collect the liquid drop, can effectively improve and draw the effect, obtains the product that purity is higher. By arranging the throat pipe 11 and arranging the demister on the throat pipe 11, after the feed liquid and the steam are in countercurrent contact and steam stripping, the flow velocity is suddenly changed when the feed liquid passes through the throat pipe 11, and the mixing effect is further enhanced. The inventor verifies through multiple experiments that after the throat pipe 11 is arranged, the product yield can be improved by 0.5-2.4%, and the yield can be improved by 3% -5%.
The utility model can realize continuous steam stripping of materials, and has good steam stripping effect and higher product yield.
Finally, it is noted that the above-mentioned preferred embodiments illustrate rather than limit the utility model, and that, although the utility model has been described in detail with reference to the above-mentioned preferred embodiments, it will be understood by those skilled in the art that various changes in form and detail may be made therein without departing from the scope of the utility model as defined by the appended claims.
Claims (4)
1. A continuous stripping apparatus, characterized by: comprises a stripping tower (1), a feed liquid tank (2), a feed liquid pump (3), a heater (4), a condenser (5) and a finished product tank (6); a feed liquid spraying system (7) is arranged in the middle of the stripping tower (1), a steam coil pipe (8) is arranged at the bottom of the stripping tower, and a demister is arranged at the top of the stripping tower; the feed liquid tank (2) is connected between the bottom of the stripping tower (1) and an inlet of the feed liquid pump (3); an outlet pipe of the feed liquid pump (3) is communicated to a feed liquid spraying system (7); the heater (4) is arranged between the feed liquid pump (3) and the feed liquid spraying system (7); the inlet of the condenser (5) is communicated with a gas phase pipeline at the top of the stripping tower (1); and the finished product tank (6) is communicated with an outlet pipe of the condenser (5).
2. A continuous stripping apparatus according to claim 1, characterized in that: the demister comprises an upper defoaming plate (9) and a lower defoaming plate (10), the upper defoaming plate and the lower defoaming plate are arranged in two layers, the upper defoaming plate (9) is an S-shaped defoaming plate, and the lower defoaming plate (10) is a grid-shaped defoaming plate.
3. A continuous stripping apparatus according to claim 2, characterized in that: a throat pipe (11) is arranged on the feed liquid spraying system (7) of the stripping tower (1); the demister is arranged above the throat (11).
4. A continuous stripping apparatus according to claim 1 or 3, characterized in that: the spray head of the feed liquid spray system (7) is a spiral spray head.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122674220.0U CN216236914U (en) | 2021-11-03 | 2021-11-03 | Continuous steam stripping device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122674220.0U CN216236914U (en) | 2021-11-03 | 2021-11-03 | Continuous steam stripping device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216236914U true CN216236914U (en) | 2022-04-08 |
Family
ID=80994947
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122674220.0U Active CN216236914U (en) | 2021-11-03 | 2021-11-03 | Continuous steam stripping device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216236914U (en) |
-
2021
- 2021-11-03 CN CN202122674220.0U patent/CN216236914U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205145645U (en) | Hypergravity revolving bed device and hypergravity rectification plant who constitutes thereof | |
| CN204756853U (en) | Pure steam generator | |
| CN104370740A (en) | Production method of isobornyl acetate | |
| CN216236914U (en) | Continuous steam stripping device | |
| CN105884586B (en) | A kind of method and device thereof of methanol gas phase dewatering preparing dimethy ether device combined production of methanol sodium | |
| CN207605386U (en) | A kind of rectifying column | |
| CN213790038U (en) | Pressure swing rectification device of methyl acetate and methyl alcohol | |
| CN107551586B (en) | Device for producing methanol by utilizing bulkhead tower to combine multiple-effect rectification | |
| CN106554270A (en) | A kind of processing method of monoxone by-product crystalline mother solution | |
| CN209464624U (en) | A kind of 2,2- dimethoxy propane continuous rectification apparatus | |
| CN208356129U (en) | A kind of mocromembrane evaporator and the distillation system comprising mocromembrane evaporator | |
| CN100569725C (en) | Formaldehyde absorbing method and system | |
| CN206721160U (en) | A kind of filler deodorizing tower for grease post processing | |
| CN204767471U (en) | With high -temperature gas concentrate system all | |
| CN202020929U (en) | Jet type solution evaporation concentration device | |
| CN105418369B (en) | The separator and method of glycerine and methyl alcohol are produced in a kind of biodiesel processes | |
| CN201643759U (en) | Efficient alcohol recovery concentrator | |
| CN204173941U (en) | Horizontal tube falling film thermocompression distiller | |
| CN104147800B (en) | Two-stage methanol evaporation column and methanol evaporation technology method | |
| CN104606913A (en) | Device for recovering solvents of explosive modeling powder water suspension granulation process | |
| CN104829452B (en) | Energy-saving production system of ethyl acetate and corresponding energy-saving production technology | |
| CN210057831U (en) | Device for utilizing waste heat of tail gas generated in synthesis of alkylpyridine | |
| CN202272798U (en) | Climbing film and falling film type multi-effect water distillator | |
| CN206188685U (en) | Device by methyl alcohol preparation formaldehyde | |
| CN218221126U (en) | Batch extractive distillation device with intermediate tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |