CN216864104U - Distillation device for turpentine - Google Patents
Distillation device for turpentine Download PDFInfo
- Publication number
- CN216864104U CN216864104U CN202121540571.6U CN202121540571U CN216864104U CN 216864104 U CN216864104 U CN 216864104U CN 202121540571 U CN202121540571 U CN 202121540571U CN 216864104 U CN216864104 U CN 216864104U
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- Prior art keywords
- distillation
- steam
- turpentine
- area
- oil
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- 238000004821 distillation Methods 0.000 title claims abstract description 67
- 241000779819 Syncarpia glomulifera Species 0.000 title claims abstract description 22
- 239000001739 pinus spp. Substances 0.000 title claims abstract description 22
- 229940036248 turpentine Drugs 0.000 title claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 45
- 238000010438 heat treatment Methods 0.000 claims abstract description 26
- 230000008018 melting Effects 0.000 claims description 2
- 238000002844 melting Methods 0.000 claims description 2
- 238000003756 stirring Methods 0.000 abstract description 13
- 239000001293 FEMA 3089 Substances 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 description 10
- 238000007599 discharging Methods 0.000 description 9
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 5
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 5
- 238000009835 boiling Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 5
- 239000004519 grease Substances 0.000 description 4
- 230000009286 beneficial effect Effects 0.000 description 2
- 239000012943 hotmelt Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000001256 steam distillation Methods 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002932 luster Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
Images
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distillation device for turpentine, which comprises a device shell and a distillation area, wherein a driving motor is arranged above the device shell, the bottom of the driving motor is connected with a driving rod, the surface of the driving rod is connected with a stirring rod, one side of the stirring rod is connected with a heating ring, a condenser is arranged above the distillation area, one side of the condenser is connected with a connecting pipe, one side of the connecting pipe is connected with an oil-water separator, one side of the oil-water separator is connected with a drain pipe, the bottom of the drain pipe is provided with a steam area, the center of the steam area is provided with a discharge hole, and heating blocks are arranged around the steam area. The distillation device for turpentine oil adopts steam to distill turpentine oil, the turpentine oil and water are not mutually soluble, the temperature of the distillation device is not required to be increased, the residual turpentine oil in the turpentine oil can be completely distilled, the cost is convenient to reduce, and the distillation efficiency is favorably improved.
Description
Technical Field
The utility model relates to the technical field of turpentine processing, in particular to a distillation device for turpentine.
Background
The distillation is a thermodynamic separation process, which utilizes the different boiling points of each component in a mixed liquid or liquid-solid system to evaporate low-boiling components and condense the low-boiling components to separate the whole components, and is a combination of two unit operations of evaporation and condensation, and in the existing rosin production line, the separation of substances is realized by a distillation method in the production process, but the rosin distillation device in the market at present has the following problems:
1. if the direct distillation is adopted for processing the turpentine, turpentine cannot be effectively extracted from turpentine liquid due to the high boiling point of the turpentine, once the temperature of a distillation device is increased, the cost is increased, the color of the produced rosin is deepened, even cracking is locally generated, and the quality is not ensured;
2. in the process of steam distillation, water needs to be converted into steam, workers need to add water for a long time, the utilization rate of water resources is not high, water resources are wasted, and a lot of workload is invisibly increased for the workers.
Aiming at the problems, the novel distillation device is innovatively designed on the basis of the original distillation device.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a distillation device for turpentine oil, which aims to solve the problems that direct distillation is adopted in the prior art for processing turpentine in the market, the turpentine oil cannot be effectively extracted from turpentine liquid due to the high boiling point of the turpentine, once the temperature of the distillation device is increased, the cost is increased, the color and luster of the produced rosin are deepened, even the rosin is cracked locally, the quality is not ensured, water needs to be converted into steam in the steam distillation process, long-term water addition is needed for workers, the utilization rate of water resources is not high, water resources are wasted, and a lot of workload is invisibly increased for the workers.
In order to achieve the purpose, the utility model provides the following technical scheme: the utility model provides a distillation plant for turpentine oil, includes device shell and distillation area, device shell top is provided with driving motor, and the driving motor bottom is connected with the actuating lever, actuating lever surface connection has the puddler, and puddler one side is connected with the heating ring, the distillation area top is provided with the condenser, and condenser one side is connected with the connecting pipe to connecting pipe one side is connected with oil water separator, oil water separator one side is connected with the drain pipe, and the drain pipe bottom is provided with steam zone to the steam zone center is provided with the discharge gate, steam zone is provided with the heating piece all around.
Preferably, the connected mode of driving motor and actuating lever is the key-type connection, and the even equidistance distribution in actuating lever bottom has the puddler to the central point of puddler coincides with the central point of heating ring.
Preferably, the oil-water separator and the drain pipe are connected in a hot melting mode, and the bottom of the drain pipe is located at the bottom of the steam area.
Preferably, the discharge port is connected with the distillation zone in a clamping manner, and the center point of the discharge port is located at the center point of the distillation zone and is superposed.
Preferably, the heating blocks are uniformly and equidistantly distributed around the steam zone, and the steam zone is positioned below the distillation zone.
Preferably, the condenser is located distillation zone top, and the even equidistance in condenser both sides distributes and has the connecting pipe to the connected mode of connecting pipe and oil water separator is fixed connection.
Compared with the prior art, the utility model has the beneficial effects that: the distillation device for the turpentine oil,
1. the device adopts steam to distill the turpentine, the turpentine and water are not mutually soluble, the temperature of the distilling device is not required to be increased, the residual turpentine in the resin liquid can be completely distilled, the cost is convenient to reduce, and the distilling efficiency is favorably improved;
2. the drain pipe is arranged on one side of the oil-water separator, and the bottom of the drain pipe is connected with the inside of the steam area, so that separated water is converted into steam again, water resources are saved and utilized, and workload of workers is reduced.
Drawings
FIG. 1 is a schematic view of the overall front view structure of the present invention;
FIG. 2 is a schematic top view of a heating ring and a stirring rod according to the present invention;
FIG. 3 is a schematic top view of the present invention;
FIG. 4 is a schematic perspective view of a heating ring and a stirring rod according to the present invention.
In the figure: 1. a device housing; 2. a drive motor; 3. an oil-water separator; 4. a connecting pipe; 5. a drive rod; 6. a drain pipe; 7. a discharge port; 8. a vapor zone; 9. a heating block; 10. a heating ring; 11. a distillation zone; 12. a condenser; 13. a stirring rod.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1-3, a distilling apparatus for turpentine comprises an apparatus housing 1 and a distilling region 11, in order to heat the fat liquid more thoroughly and facilitate rapid distillation, a driving motor 2 is disposed above the apparatus housing 1, a driving rod 5 is connected to the bottom of the driving motor 2, a stirring rod 13 is connected to the surface of the driving rod 5, a heating ring 10 is connected to one side of the stirring rod 13, the driving motor 2 is connected to the driving rod 5 in a key connection manner, the stirring rods 13 are uniformly and equidistantly distributed at the bottom of the driving rod 5, the center point of the stirring rod 13 is coincident with the center point of the heating ring 10, the driving motor 2 is turned on, the driving rod 5 drives the driving rod 5 to rotate, the driving rod 5 drives the stirring rod 13 to rotate and simultaneously drives the heating ring 10 to rotate, the driving motor 2 is connected to the driving rod 5 in a key connection manner, and the stirring rods 13 are uniformly and equidistantly distributed at the bottom of the driving rod 5, and the central point of the stirring rod 13 coincides with the central point of the heating ring 10, which is beneficial to heating the fat liquid and is convenient for improving the distillation efficiency.
Referring to fig. 1-4, in order to reuse water resources, a drain pipe 6 is connected to one side of the oil-water separator 3, a steam area 8 is disposed at the bottom of the drain pipe 6, the oil-water separator 3 is connected to the drain pipe 6 in a hot-melt manner, and the bottom of the drain pipe 6 is located at the bottom of the steam area 8, when the oil-water separator 3 separates oil from water, water flows along the drain pipe 6 and falls into the steam area 8 at the bottom, and is heated by a heating block 9 and then converted into steam again, and then enters a distillation area 11 again, the oil-water separator 3 is connected to the drain pipe 6 in a hot-melt manner, and the bottom of the drain pipe 6 is located at the bottom of the steam area 8, so that water resources can be recycled, cost can be saved, and workload of workers can be reduced.
Referring to fig. 1-4, in order to facilitate discharging, a discharging port 7 is disposed in the center of the steam zone 8, the discharging port 7 is connected to the distillation zone 11 in a snap-fit manner, and a central point of the discharging port 7 is located at a center of the distillation zone 11 and coincides with the center point of the distillation zone 11, after the distillation is completed, the discharging port 7 is opened, the remaining objects are discharged from the discharging port 7, the discharging port 7 is connected to the distillation zone 11 in a snap-fit manner, and the central point of the discharging port 7 is located at a center of the distillation zone 11 and coincides with the center point of the distillation zone 11, so that rapid discharging is facilitated, and operation of workers is facilitated.
Referring to fig. 1-4, in order to increase the distillation speed, a condenser 12 is disposed above the distillation area 11, a connecting pipe 4 is connected to one side of the condenser 12, an oil-water separator 3 is connected to one side of the connecting pipe 4, heating blocks 9 are uniformly and equidistantly distributed around the steam area 8, the steam area 8 is located below the distillation area 11, the condenser 12 is located above the distillation area 11, connecting pipes 4 are uniformly and equidistantly distributed on two sides of the condenser 12, the connecting pipes 4 are fixedly connected to the oil-water separator 3, when the heating blocks 9 start to operate, water in the steam area 8 is heated to be steam, and then flows into the distillation area 11, and meanwhile, the steam area 8 is located below the distillation area 11, the distillation area 11 is heated during the rising of the steam, and then flows into the condenser 12 after the distillation is completed, and then flows into the oil-water separator 3 through the connecting pipe 4, the even equidistance of heating block 9 distributes around steam zone 8, and steam zone 8 is located 11 below in distillation zone, is convenient for add hot water vapor, improves distillation speed simultaneously, and condenser 12 is located 11 tops in distillation zone, and the even equidistance in condenser 12 both sides distributes and has connecting pipe 4 to connecting pipe 4 is fixed connection with oil water separator 3's connected mode, is favorable to improving work efficiency, and the device automation of being convenient for moves.
The working principle is as follows: according to the figures 1-4, when the heating block 9 starts to work, water in the steam zone 8 is heated into steam, then the steam flows into the distillation zone 11, meanwhile, the steam zone 8 is positioned below the distillation zone 11, the distillation zone 11 is heated in the process of rising of the steam, the driving motor 2 is started, the driving rod 5 is driven to rotate by the driving motor 2, the stirring rod 13 is driven to rotate by the driving rod 5, the heating ring 10 is driven to rotate at the same time, the distillation speed of the grease liquid is accelerated, the grease liquid is heated for the second time, the grease liquid enters the condenser 12 after the distillation is finished, and then the grease liquid enters the oil-water separator 3 through the connecting pipe 4;
according to fig. 1-4, after the oil-water separator 3 separates the oil and water, the water flow is discharged along the water discharge pipe 6, falls into the steam zone 8 at the bottom, is heated by the heating block 9 and then is converted into water vapor again, and enters the distillation zone 11 again, which is the working process of the whole device, and the content not described in detail in the present specification belongs to the prior art known to those skilled in the art.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the utility model, the scope of which is defined in the appended claims and their equivalents.
Claims (6)
1. A distillation apparatus for turpentine comprising an apparatus housing (1) and a distillation zone (11), characterized in that: device shell (1) top is provided with driving motor (2), and driving motor (2) bottom is connected with actuating lever (5), actuating lever (5) surface connection has puddler (13), and puddler (13) one side is connected with heating ring (10), distillation zone (11) top is provided with condenser (12), and condenser (12) one side is connected with connecting pipe (4) to connecting pipe (4) one side is connected with water oil separator (3), water oil separator (3) one side is connected with drain pipe (6), and drain pipe (6) bottom is provided with steam zone (8) to steam zone (8) center is provided with discharge gate (7), steam zone (8) are provided with heating block (9) all around.
2. The distillation apparatus for turpentine according to claim 1, wherein: the connection mode of driving motor (2) and actuating lever (5) is the key-type connection, and actuating lever (5) bottom uniform spacing distributes has puddler (13) to the central point of puddler (13) and the coincidence of the central point of heating ring (10).
3. A distillation apparatus for turpentine according to claim 2, wherein: the oil-water separator (3) is connected with the drain pipe (6) in a hot melting mode, and the bottom of the drain pipe (6) is located at the bottom of the steam area (8).
4. A distillation apparatus for turpentine according to claim 3, wherein: the discharge port (7) is connected with the distillation area (11) in a clamping manner, and the central point of the discharge port (7) is positioned at the central point of the distillation area (11) and is superposed.
5. A distillation apparatus for turpentine according to claim 2, wherein: the heating blocks (9) are uniformly distributed around the steam area (8) in equal intervals, and the steam area (8) is positioned below the distillation area (11).
6. A distillation apparatus for turpentine according to claim 2, wherein: condenser (12) are located distillation zone (11) top, and condenser (12) both sides uniform distance distributes has connecting pipe (4) to the connected mode of connecting pipe (4) and oil water separator (3) is fixed connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121540571.6U CN216864104U (en) | 2021-07-07 | 2021-07-07 | Distillation device for turpentine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121540571.6U CN216864104U (en) | 2021-07-07 | 2021-07-07 | Distillation device for turpentine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216864104U true CN216864104U (en) | 2022-07-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121540571.6U Expired - Fee Related CN216864104U (en) | 2021-07-07 | 2021-07-07 | Distillation device for turpentine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216864104U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228122A (en) * | 2022-07-15 | 2022-10-25 | 广西上林县林发松香有限公司 | High-efficiency energy-saving distillation tower and method for extracting rosin and turpentine |
-
2021
- 2021-07-07 CN CN202121540571.6U patent/CN216864104U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115228122A (en) * | 2022-07-15 | 2022-10-25 | 广西上林县林发松香有限公司 | High-efficiency energy-saving distillation tower and method for extracting rosin and turpentine |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20220701 |
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| CF01 | Termination of patent right due to non-payment of annual fee |