CN205205066U - Device for extracting turpentine from middle -layer resin liquid - Google Patents
Device for extracting turpentine from middle -layer resin liquid Download PDFInfo
- Publication number
- CN205205066U CN205205066U CN201520877517.9U CN201520877517U CN205205066U CN 205205066 U CN205205066 U CN 205205066U CN 201520877517 U CN201520877517 U CN 201520877517U CN 205205066 U CN205205066 U CN 205205066U
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- steam
- pot
- boil water
- layer resin
- resin liquid
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Abstract
The utility model relates to a rosin processingequipment field, purpose provide a device for extracting turpentine from middle -layer resin liquid, the device ability continuous production, and the gum spirit extraction efficiency is high. A device for extracting turpentine from middle -layer resin liquid, is including boiling water pot. Boil the inside steam pipe that sets up of water pot, steam inlet connection delivery duct is stretched out to the steam pipe upper end, the lower extreme is located and boils water pot middle part connection steam distributor, boil the water pot bottom and be hourglass hopper -shaped, boil the water pot bottom outside and set up the vertical pivot of arranging of motor connection, the pivot lower part sets up oil scraping plate, upper portion sets up helical blade. The steam distributor is located the middle part, avoids appearing the phenomenon that the tallow oil blockked up steam outlet, improves the gum spirit extraction efficiency. The impurity that the oil scraping plate of pivot lower part can will glue on the inner wall strikes off, is favorable to continuous production, the helical blade on upper portion is through stirring fat liquid, is favorable to volatilizing of in fat liquid gum spirit, effectively improves the gum spirit extraction efficiency.
Description
Technical field
The utility model relates to pine gum processing device field, is specifically related to one from middle-layer resin liquid, extracts terebinthine device.
Background technology
Rosin can be processed into rosin and turps, and turps is a kind of excellent organic solvent, is widely used in the industry such as paint, siccative, tackiness agent, is pharmaceutically can be used as antitoxin, cutaneous stimulant etc.In the course of processing of rosin, be first delivered in dissolving pan by rosin and melt, melt fat liquid and enter clarifying kettle clarification, that is left after reclaiming turps is middle-layer resin liquid.In these in layer fat liquid except the inferior rosin of moisture, fine impurities and dead color, still containing part turps.
For the recovery of middle-layer resin liquid, part factory adopts the mode left standstill.Stratification in the great Chi being discharged into a lot of and many lattice by middle-layer resin liquid.This process depending merely on fat liquid natural layering is slow, and actual in the middle of layered effect undesirable, still waste the too much resources of production.CN202157047U discloses one from middle-layer resin liquid, extracts terebinthine device.Utilize the steam of input to carry out hot digestion, vaporous turps and water vapor are reclaimed by turps recovery tube together.But this device is batch production, after boiling, carry out the operation such as draining, deslagging again.And vapour pipe is positioned at pot bottom to boil water, the steam hole on vapour pipe, especially near the steam hole of bottom, easily there is the problem blocked, affect boiling and carry out smoothly, reduce extraction efficiency.
Summary of the invention
The purpose of this utility model is to provide one from middle-layer resin liquid, extracts terebinthine device, and this device energy continuous seepage, turps extraction efficiency is high.
For achieving the above object, the technical scheme that the utility model adopts is: one extracts terebinthine device from middle-layer resin liquid, and comprise pot to boil water, pot top to boil water arranges opening for feed.Described pot top to boil water arranges steam inlet and discharge port, and bottom arranges slag-drip opening and water vent; Described pot inside to boil water arranges vapour pipe; Steam inlet connection steam pipeline is stretched out in described vapour pipe upper end, lower end is positioned in the middle part of pot to boil water and connects steam distributor;
Described pot bottom to boil water is funnel-form, the rotating shaft that pot bottom arranged outside motor vertical connecting to boil water is arranged, rotating shaft is stretched in tank body; It is described that rotating shaft bottom arranges oil scraping plate, top arranges screw-blade.
Further: described steam distributor is disk or is made up of the outward extending many steam outlet pipes of the even divergent shape in vapour pipe lower end; Described disk or steam outlet pipe evenly arrange steam hole.
Further: the lower surface of described disk or steam outlet pipe evenly arranges steam hole.
Further: described pot top to boil water arranges porthole.
Further: described pot top to boil water arranges evacuation port.
Further: described evacuation port connects two evacuated tube, evacuated tube and lower evacuated tube is respectively; Described lower evacuated tube extends layout downwards, and lower end is arrived close to ground location; Described upper evacuated tube installs automatic blow off valve, lower evacuated tube installs manual valve near lower end.
The utility model has following beneficial effect: the steam distributor in pot to boil water is positioned at middle part, avoids the phenomenon occurring fatty oil blocking vapour outlet, improves turps extraction efficiency.Pot bottom to boil water is the discharge that funnel-form is conducive to impurity.The rotating shaft that pot bottom arranged outside motor vertical connecting to boil water is arranged, rotating shaft bottom arranges oil scraping plate, top arranges screw-blade.By motor connection rotating shaft, rotating shaft drives oil scraping plate and screw-blade to rotate.The impurity be bonded on inwall can strike off by the oil scraping plate of rotating shaft bottom, prevents blocking, is conducive to continuous seepage; The screw-blade on top, by stirring fat liquid, strengthens the effect of heat trnasfer, is conducive to terebinthine volatilization in fat liquid, effectively improve turps extraction efficiency.This device also can be used for rosin and melts, and highly versatile reduces equipment cost.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of steam distributor;
Fig. 3 is the upward view of steam distributor.
Embodiment
As shown in Figure 1, one extracts terebinthine device from middle-layer resin liquid, and comprise pot 1 to boil water, pot 1 top to boil water arranges opening for feed 2.Described pot to boil water 1 top arranges steam inlet 4 and discharge port 3, and bottom arranges slag-drip opening 6 and water vent 7.Described pot to boil water 1 inside arranges vapour pipe; Described vapour pipe upper end stretches out that steam inlet 4 connects steam pipeline, lower end is positioned in the middle part of pot 1 to boil water and connects steam distributor 5.In continuous flow procedure, middle-layer resin liquid continues to add from opening for feed 2, is gathered in pot 1 bottom to boil water; Superheated vapour enters pot 1 to boil water by vapour pipe; Turpentine oil volatile in middle-layer resin liquid is discharged from discharge port 3 together with water vapor.Steam distributor 5 in pot 1 to boil water is positioned at middle part, avoids the phenomenon occurring fatty oil blocking vapour outlet, improves turps extraction efficiency.
In funnel-form bottom described pot to boil water 1, pot 1 bottom outside to boil water arranges the rotating shaft 9 that motor 8 vertical connecting is arranged, rotating shaft 9 is stretched in tank body 1; Described rotating shaft 9 bottom arranges oil scraping plate 10, top arranges screw-blade 11.By motor 8 connection rotating shaft 9, rotating shaft 9 drives oil scraping plate 10 and screw-blade 11 to rotate.The impurity be bonded on inwall can strike off by the oil scraping plate 10 of rotating shaft 9 bottom, prevents blocking, is conducive to continuous seepage; The screw-blade 11 on top, by stirring fat liquid, strengthens the effect of heat trnasfer, is conducive to terebinthine volatilization in fat liquid, effectively improve turps extraction efficiency.
Described steam distributor 5 can be disk, and steam distribution amount is large, can effectively disperse entered steam.Steam hole all can be arranged in the upper and lower surface of disk, enters steam in a large number.For avoiding the steam hole of upper surface to be blocked by grease and being unfavorable for steam distribution, preferably lower disk surface is evenly arranged steam hole.Described steam distributor 5 also can be as shown in Figure 2, and steam distributor 5 is made up of the outward extending many steam outlet pipes 51 of the even divergent shape in vapour pipe lower end.As shown in Figure 3, steam hole 52 is evenly distributed on the lower surface of steam outlet pipe 51.Escape pipe 51 steam distribution amount is little, and take up space is little compared with disk, can not hinder the rising of turps and water vapor.
Described pot to boil water 1 top arranges porthole 12, the condition of production in convenient observation pot.Described pot to boil water 1 top arranges evacuation port 13.Described evacuation port 13 connects two evacuated tube, is respectively evacuated tube 14 and lower evacuated tube 15; Described lower evacuated tube 15 extends layout downwards, and lower end is arrived close to ground location; Described upper evacuated tube 14 installs automatic blow off valve, lower evacuated tube 15 installs manual valve near lower end.Evacuated tube divides upper and lower two settings, lower evacuated tube 15 according to circumstances manual control.Automatic blow off valve in upper evacuated tube 14 is in closing condition usually, only has pot inner pressure to exceed setting limit, just automatically can open and carry out emptying decompression, avoid having an accident.
Claims (6)
1. one kind is extracted terebinthine device from middle-layer resin liquid, comprise pot to boil water (1), pot to boil water (1) top arranges opening for feed (2), it is characterized in that: described pot to boil water (1) top arranges steam inlet (4) and discharge port (3), and bottom arranges slag-drip opening (6) and water vent (7); Described pot to boil water (1) inside arranges vapour pipe; Steam inlet (4) connection steam pipeline is stretched out in described vapour pipe upper end, lower end is positioned at pot to boil water (1) middle part and connects steam distributor (5);
Described pot to boil water (1) bottom is in funnel-form, and pot to boil water (1) bottom outside arranges the rotating shaft (9) that motor (8) vertical connecting is arranged, rotating shaft (9) is stretched in tank body (1); Described rotating shaft (9) bottom arranges oil scraping plate (10), top arranges screw-blade (11).
2. one according to claim 1 extracts terebinthine device from middle-layer resin liquid, it is characterized in that: described steam distributor (5) is formed for disk or by the outward extending many steam outlet pipes (51) of the even divergent shape in vapour pipe lower end; Described disk or steam outlet pipe (51) evenly arrange steam hole (52).
3. one according to claim 2 extracts terebinthine device from middle-layer resin liquid, it is characterized in that: the lower surface of described disk or steam outlet pipe (51) evenly arranges steam hole (52).
4. the one according to claim 1 or 2 or 3 extracts terebinthine device from middle-layer resin liquid, it is characterized in that: described pot to boil water (1) top arranges porthole (12).
5. the one according to claim 1 or 2 or 3 extracts terebinthine device from middle-layer resin liquid, it is characterized in that: described pot to boil water (1) top arranges evacuation port (13).
6. one according to claim 5 extracts terebinthine device from middle-layer resin liquid, it is characterized in that: described evacuation port (13) connects two evacuated tube, is respectively evacuated tube (14) and lower evacuated tube (15); Described lower evacuated tube (15) extends layout downwards, and lower end is arrived close to ground location; Described upper evacuated tube (14) installs automatic blow off valve, and lower evacuated tube (15) is upper installs manual valve near lower end.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520877517.9U CN205205066U (en) | 2015-11-06 | 2015-11-06 | Device for extracting turpentine from middle -layer resin liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520877517.9U CN205205066U (en) | 2015-11-06 | 2015-11-06 | Device for extracting turpentine from middle -layer resin liquid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205205066U true CN205205066U (en) | 2016-05-04 |
Family
ID=55842794
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520877517.9U Expired - Fee Related CN205205066U (en) | 2015-11-06 | 2015-11-06 | Device for extracting turpentine from middle -layer resin liquid |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205205066U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355370A (en) * | 2017-07-01 | 2018-08-03 | 石城县松湖林业化工有限公司 | A kind of turpentine oil processing distilling apparatus |
-
2015
- 2015-11-06 CN CN201520877517.9U patent/CN205205066U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108355370A (en) * | 2017-07-01 | 2018-08-03 | 石城县松湖林业化工有限公司 | A kind of turpentine oil processing distilling apparatus |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160504 Termination date: 20161106 |