CN206396160U - A kind of essence MNO purification by liquid extraction drying devices - Google Patents
A kind of essence MNO purification by liquid extraction drying devices Download PDFInfo
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- CN206396160U CN206396160U CN201621451070.XU CN201621451070U CN206396160U CN 206396160 U CN206396160 U CN 206396160U CN 201621451070 U CN201621451070 U CN 201621451070U CN 206396160 U CN206396160 U CN 206396160U
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- mno
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- extraction
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Abstract
The utility model discloses a kind of essence MNO purification by liquid extraction drying devices, including extraction equipment and conveying device, the left bottom of the extraction equipment is communicated in the left side top of conveying device by drainage conduit, the second valve is provided with the mouth of pipe of the drainage conduit, the right-hand member of the conveying device extends through purifying plant and drying device, the top of the purifying plant is connected by evaporation tube with the bottom right of cooling device, the bottom left of the cooling device passes through extraction equipment by the return duct device that is connected with the top right side of extraction equipment, conveying device, purifying plant, the setting of drying device and cooling device, so that the extraction of MNO crystal is quicker, improve the production efficiency of MNO crystal, conveyed by the straight line of conveying device, reduce the loss of MNO crystal.
Description
Technical field
The utility model is related to essence production equipment technical field, specially a kind of essence MNO purification by liquid extraction drying devices.
Background technology
Essence is by the artificial synthesized concentration aromatic oil for imitating fruit and natural perfume material smell.It is a kind of artificial musk
Material.It is used for manufacturing food, cosmetics and cigarette etc..Essence MNO needs to carry out purification by liquid extraction and drying in process of production, existing
Some essence MNO purification by liquid extractions and drying device low production efficiency, cause into production cost increase, are unfavorable for the popularization of equipment, are
This, proposes a kind of essence MNO purification by liquid extraction drying devices.
Utility model content
The purpose of this utility model is to provide a kind of essence MNO purification by liquid extraction drying devices, to solve above-mentioned background skill
The problem of being proposed in art.
To achieve the above object, the utility model provides following technical scheme：A kind of essence MNO purification by liquid extractions dry dress
Put, including extraction equipment and conveying device, the left bottom of the extraction equipment is communicated in a left side for conveying device by drainage conduit
The second valve is provided with side roof part, the mouth of pipe of the drainage conduit, the right-hand member of the conveying device extends through purifying plant and dry
Dry device, the top of the purifying plant is connected by evaporation tube with the bottom right of cooling device, the cooling device
Bottom left is connected by return duct with the top right side of extraction equipment.
It is preferred that, the extraction equipment includes extraction tower, and the top left and right sides of the extraction tower has been respectively communicated with charging
Mouth and return duct, the left bottom of the extraction tower are communicated with drainage conduit.
It is preferred that, the conveying device includes delivery pipe, and the outer left side of the delivery pipe is provided with motor, the motor
The rotating shaft through delivery pipe is connected with, the outside of the rotating shaft is provided with helical-blade, and the outside top of the delivery pipe uniformly runs through
There is through hole, the through hole is located at the inside of purifying plant and drying device respectively, and the bottom right side of the delivery pipe is provided with filter screen,
The filter screen is located at the inside of drying device.
It is preferred that, the purifying plant includes purification case, and the top of the purification case is connected with evaporation tube, the purification
The bottom of case is provided with the heating plate of internal sandwiched heater strip, top and the conveying device close proximity of the heating plate.
It is preferred that, the drying device includes drying box, and the top left and right sides of the drying box has been respectively communicated with first
Pipeline and second pipe, the bottom of the drying box, which is communicated with discharge nozzle, the mouth of pipe of the discharge nozzle, is provided with the first valve.
It is preferred that, the cooling device includes cooler bin, the left and right sides of the cooler bin be respectively communicated with water inlet and
Delivery port, the bottom left and right sides of the cooler bin has extended through return duct and evaporation tube, the top right side of the return duct
The top left side of evaporation tube is communicated in by heat exchanger tube, and the quantity of heat exchanger tube is no less than four.
Compared with prior art, the beneficial effects of the utility model are：The device by extraction equipment, conveying device, carry
The setting of pure device, drying device and cooling device so that the extraction of MNO crystal is quicker, improves the production of MNO crystal
Efficiency, is conveyed by the straight line of conveying device, reduces the loss of MNO crystal.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Fig. 2 is the utility model extraction equipment structural representation；
Fig. 3 is the utility model transport conveyor constructions schematic diagram；
Fig. 4 is the utility model purifying plant structural representation；
Fig. 5 is the utility model drying device structural representation；
Fig. 6 is the utility model cooling device structural representation.
In figure：1 extraction equipment, 2 conveying devices, 3 purifying plants, 4 drying devices, 5 cooling devices, 6 evaporation tubes, 7 backflows
Pipe, 8 drainage conduits, 9 first valves, 10 extraction towers, 11 charging apertures, 12 delivery pipes, 13 motors, 14 rotating shafts, 15 helical-blades, 16 filters
Net, 17 through holes, 18 purification casees, 19 heating plates, 20 first pipelines, 21 second pipes, 22 discharge nozzles, 23 cooler bins, 24 heat exchanger tubes,
25 water inlets, 26 delivery ports, 27 second valves, 28 drying boxes.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Fig. 1-6 are referred to, the utility model provides a kind of technical scheme：A kind of essence MNO purification by liquid extraction drying devices, bag
Extraction equipment 1 and conveying device 2 are included, the left bottom of the extraction equipment 1 is communicated in a left side for conveying device 2 by drainage conduit 8
The second valve 27 is provided with side roof part, the mouth of pipe of the drainage conduit 8, the right-hand member of the conveying device 2 extends through purifying plant 3
With drying device 4, the top of the purifying plant 3 is connected by evaporation tube 6 with the bottom right of cooling device 5, described cold
But the bottom left of device 5 is connected by return duct 7 with the top right side of extraction equipment 1.
Further, the extraction equipment 1 includes extraction tower 10, and the top left and right sides of the extraction tower 10 is respectively communicated with
There are charging aperture 11 and return duct 7, the left bottom of the extraction tower 10 is communicated with drainage conduit 8, for being extracted to MNO.
Further, the conveying device 2 includes delivery pipe 12, and the outer left side of the delivery pipe 12 is provided with motor
13, the motor 13 is connected with the rotating shaft 14 through delivery pipe 12, and the outside of the rotating shaft 14 is provided with helical-blade 15, the conveying
The outside top of pipe 12 is uniformly through there is through hole 17, and the through hole 17 is located at the inside of purifying plant 3 and drying device 4 respectively,
The bottom right side of the delivery pipe 12 is provided with filter screen 16, and the filter screen 16 is located at the inside of drying device 4, is mixed for conveying MNO
It is fit.
Further, the purifying plant 3 includes purification case 18, and the top of the purification case 18 is connected with evaporation tube 6,
The bottom of the purification case 18 is provided with the heating plate 19 of internal sandwiched heater strip, top and the conveying device 2 of the heating plate 19
Close proximity, for being evaporated to MNO mixtures.
Further, the drying device 4 includes drying box 28, and the top left and right sides of the drying box 28 is respectively communicated with
There are the first pipeline 20 and second pipe 21, the bottom of the drying box 28 is communicated with discharge nozzle 22, the mouth of pipe of the discharge nozzle 22
Place is provided with the first valve 9, for being dried to MNO crystal.
Further, the cooling device 5 includes cooler bin 23, the left and right sides of the cooler bin 23 be respectively communicated with into
The mouth of a river 25 and delivery port 26, the bottom left and right sides of the cooler bin 23 have extended through return duct 7 and evaporation tube 6, described time
The top right side of flow tube 7 is communicated in the top left side of evaporation tube 6 by heat exchanger tube 24, and the quantity of heat exchanger tube 24 is no less than four
It is individual, for being cooled down to gas.
Specifically, in use, MNO raw materials and extract ethyl acetate are knocked down in extraction tower 10 with extracting from charging aperture 11
Liquid ethyl acetate is mixed, and the second valve 27 is opened after the completion of extraction so that mixing liquid enters in delivery pipe 12 from drainage conduit 8,
Start motor 13 simultaneously so that motor 13 drives rotating shaft 14 to rotate, rotating shaft 14 drives helical-blade 15 to rotate, so as to drive mixed liquor
Body is conveyed to the right, and during the purified device 3 of mixing liquid, mixing liquid can evaporate under the high-temperature heating of heating plate 19, evaporation
Gas enters in evaporation tube 6 from through hole 17, while injecting cold water to water inlet 25, cold water flows out from delivery port 26, the vapour of evaporation
Body enters heat exchanger tube 24 from evaporation tube 6, and enters return duct 7 from heat exchanger tube 24, and now gas is cooled into liquid, then liquid
It is back in extraction tower 10, the mixing liquid after being evaporated can be crystallized, forms the mixture with crystallization, mixture is in spiral shell
Continue to move right under the drive of vane 15, mixture enters in drying device 4, and liquid can fall into drying box 28 from filter screen 16
Bottom, while discharging into high-temperature gas to the first pipeline 20, high-temperature gas is discharged from second pipe 21, and high-temperature gas is by MNO crystal
Dried, the MNO crystal after drying is discharged under the drive of helical-blade 15 from the right-hand member of delivery pipe 12, into drying box 28
Liquid can again be extracted by opening the taking-up of the first valve 9.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of essence MNO purification by liquid extraction drying devices, including extraction equipment (1) and conveying device (2), it is characterised in that：Institute
The left bottom for stating extraction equipment (1) is communicated in the left side top of conveying device (2), the drainage conduit (8) by drainage conduit (8)
The mouth of pipe at be provided with the second valve (27), the right-hand member of the conveying device (2) extends through purifying plant (3) and drying device
(4), the top of the purifying plant (3) is connected by evaporation tube (6) with the bottom right of cooling device (5), the cooling
The bottom left of device (5) is connected by return duct (7) with the top right side of extraction equipment (1).
2. a kind of essence MNO purification by liquid extraction drying devices according to claim 1, it is characterised in that：The extraction equipment
(1) extraction tower (10) is included, the top left and right sides of the extraction tower (10) has been respectively communicated with charging aperture (11) and return duct
(7), the left bottom of the extraction tower (10) is communicated with drainage conduit (8).
3. a kind of essence MNO purification by liquid extraction drying devices according to claim 1, it is characterised in that：The conveying device
(2) delivery pipe (12) is included, the outer left side of the delivery pipe (12) is provided with motor (13), and the motor (13), which is connected with, passes through
The rotating shaft (14) of delivery pipe (12) is worn, the outside of the rotating shaft (14) is provided with helical-blade (15), the outside of the delivery pipe (12)
Top is uniformly through there is through hole (17), and the through hole (17) is located at the inside of purifying plant (3) and drying device (4), institute respectively
The bottom right side for stating delivery pipe (12) is provided with filter screen (16), and the filter screen (16) is located at the inside of drying device (4).
4. a kind of essence MNO purification by liquid extraction drying devices according to claim 1, it is characterised in that：The purifying plant
(3) purification case (18) is included, the top of the purification case (18) is connected with evaporation tube (6), the bottom of the purification case (18)
Heating plate (19) provided with internal sandwiched heater strip, top and conveying device (2) close proximity of the heating plate (19).
5. a kind of essence MNO purification by liquid extraction drying devices according to claim 1, it is characterised in that：The drying device
(4) drying box (28) is included, the top left and right sides of the drying box (28) has been respectively communicated with the first pipeline (20) and the second pipe
Road (21), the bottom of the drying box (28), which is communicated with discharge nozzle (22), the mouth of pipe of the discharge nozzle (22), is provided with the first valve
Door (9).
6. a kind of essence MNO purification by liquid extraction drying devices according to claim 1, it is characterised in that：The cooling device
(5) cooler bin (23) is included, the left and right sides of the cooler bin (23) has been respectively communicated with water inlet (25) and delivery port (26), institute
The bottom left and right sides for stating cooler bin (23) has extended through return duct (7) and evaporation tube (6), the top of the return duct (7)
Right side is communicated in the top left side of evaporation tube (6) by heat exchanger tube (24), and the quantity of heat exchanger tube (24) is no less than four.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621451070.XU CN206396160U (en) | 2016-12-28 | 2016-12-28 | A kind of essence MNO purification by liquid extraction drying devices |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621451070.XU CN206396160U (en) | 2016-12-28 | 2016-12-28 | A kind of essence MNO purification by liquid extraction drying devices |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206396160U true CN206396160U (en) | 2017-08-11 |
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ID=59517318
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621451070.XU Active CN206396160U (en) | 2016-12-28 | 2016-12-28 | A kind of essence MNO purification by liquid extraction drying devices |
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| Country | Link |
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| CN (1) | CN206396160U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108034496A (en) * | 2017-12-12 | 2018-05-15 | 梁林燕 | A kind of production of flavor device with high extraction |
| CN115350495A (en) * | 2022-08-19 | 2022-11-18 | 焦作市馨之源科技有限公司 | Equipment and process for extracting sclareol |
-
2016
- 2016-12-28 CN CN201621451070.XU patent/CN206396160U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108034496A (en) * | 2017-12-12 | 2018-05-15 | 梁林燕 | A kind of production of flavor device with high extraction |
| CN115350495A (en) * | 2022-08-19 | 2022-11-18 | 焦作市馨之源科技有限公司 | Equipment and process for extracting sclareol |
| CN115350495B (en) * | 2022-08-19 | 2023-11-21 | 焦作市馨之源科技有限公司 | Equipment and process for extracting sclareol |
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