CN206033660U - Gum spirit distillation apparatus for producing - Google Patents
Gum spirit distillation apparatus for producing Download PDFInfo
- Publication number
- CN206033660U CN206033660U CN201621024826.2U CN201621024826U CN206033660U CN 206033660 U CN206033660 U CN 206033660U CN 201621024826 U CN201621024826 U CN 201621024826U CN 206033660 U CN206033660 U CN 206033660U
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- CN
- China
- Prior art keywords
- cooling
- stirring
- stirring distillation
- distillation reaction
- reaction tank
- 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.)
- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a gum spirit distillation apparatus for producing, including stirring distillation reactor jar, cooling device, the oil -water separator who communicates in proper order, stirring distillation reactor tank bottoms portion is provided with the heating furnace, be connected with driving motor on the stirring distillation reactor jar, in the driving motor output shaft stretched into stirring distillation reactor jar, just end connection had the axle sleeve on the output shaft, and the axle sleeve periphery is provided with a plurality of bar slots to there is stirring paddle leaf at the slot in -connection, steam flow hole passes through the drainage tube and communicates cooling device, cooling device includes enclosed housing, and the shell intussuseption is filled with the coolant liquid, still have the cooling coil subassembly through the support mounting in the shell, coil assembly is provided with many cooling tubes, and many cooling tubes lead to turn the corner and communicate the circuitous return circuit of formation in proper order for first two liang to be provided with a plurality of heat exchanger plates on the every cooling tube periphery. Adopt the utility model discloses can effectively improve the condensation effect, avoid extravagant.
Description
Technical field
The utility model is related to rosin manufacture field, and in particular to a kind of turpentine oil distills process units.
Background technology
Existing turpentine oil production technology is by entering boiler after will be Oleoresin preheated, being added with indirect water vapour
Heat, then be directly passed through water vapour into boiler and do working steam stirring fat liquid, under the conditions of being heated to uniform temperature, steam from boiler
Water and terebinthine mixed vapour, then condensation separation.But carry out heating by vapor the method for distillation in later stage condensation effect
It is really poor, cause substantial amounts of waste.
Utility model content
The utility model aims to provide a kind of turpentine oil distillation process units, to solve the above problems.
For achieving the above object, the technical solution of the utility model is as follows:
A kind of turpentine oil distills process units, it is characterised in that:Including the stirring distillation reaction tank, cooling dress that are sequentially communicated
Put, oily-water seperating equipment;The stirring distillation reaction pot bottom is provided with heating furnace;It is connected with the stirring distillation reaction tank
Motor, driving motor output shaft are extend in stirring distillation reaction tank, and are connected with axle sleeve, axle sleeve in output shaft upper end
Periphery is provided with multiple bar shaped slots, and in slot is connected with stirrer paddle;At the upper side of the stirring distillation reaction tank
Steam communication port is provided with, and opposite side is provided with pressure relief opening, on pressure relief opening, be connected with blowdown piping, and on blowdown piping
It is connected with relief valve;The steam communication port is communicated to cooling device by drainage tube, and the cooling device includes closed outer
Shell, inside the shell are filled with coolant;The inside the shell is also provided with cooling coil component by support, and coil pack is provided with many
Root cooling tube, many cooling tubes are sequentially communicated to form roundabout loop by elbow two-by-two, and set on every cooling tube periphery
It is equipped with multiple heat exchanger plates;The coil pack outlet is communicated to oily-water seperating equipment, oily-water seperating equipment entrance by straight tube
Place is provided with lauter tub, and lauter tub includes tubular support and is laid on the screen pack of tubular support outer layer;The oily-water seperating equipment point
Wastewater outlet and turpentine oil export are not provided with.
Further, the stirring distillation reaction tank top is provided with seal closure.
The beneficial effects of the utility model are:Oleoresin is passed through retort in processing distillation by the utility model
It is interior, then heated to stirring distillation reaction tank by electric furnace, while being stirred to rosin using stirrer paddle, strengthen
Distilling effect.And the side of retort is provided with pressure relief opening, drastically raises when air pressure in retort is run into, can be by letting out
Pressure valve emergency opening, is directly vented.Blade is to pull and push connection, easy access.
Again, it is of the present utility model to connect to form roundabout cooling circuit, Ke Yi using elbow using many cooling tubes
Largely increase the length of cooling tube, strengthen cooling effect.
Meanwhile, the utility model is provided with lauter tub in oily-water seperating equipment entrance, and lauter tub can be with solid particulate matter and one
The impurity produced in a little production processes is filtered, and carries out periodic cleaning, the blocking in gun barrel.
Description of the drawings
Fig. 1 is the turpentine oil distillation process units structural representation that the utility model is provided.
Mark in figure:1 is stirring distillation reaction tank, 2 is heating furnace, 3 is cooling device, 4 is oily-water seperating equipment, 5 are
Motor, 6 be output shaft, 7 be stirrer paddle, 8 be drainage tube, 9 be cooling tube, 10 be heat exchanger plate, 11 be straight tube.
Specific embodiment
The utility model is described further with specific embodiment below in conjunction with the accompanying drawings.
As shown in figure 1, a kind of turpentine oil distills process units, it is characterised in that:It is anti-including the stirring distillation being sequentially communicated
Answer tank 1, cooling device 3, oily-water seperating equipment 4;1 bottom of stirring distillation reaction tank is provided with heating furnace 2;The stirring is steamed
Evaporate and in retort 1, be connected with motor 5,5 output shaft 6 of motor is extend in stirring distillation reaction tank 1, and in output shaft
6 upper ends are connected with axle sleeve, and axle sleeve periphery is provided with multiple bar shaped slots, and is connected with stirrer paddle 7 in slot;It is described
Steam communication port is provided with the upper side of stirring distillation reaction tank 1, and opposite side is provided with pressure relief opening, be connected with pressure relief opening
Blowdown piping, and relief valve is connected with blowdown piping;The steam communication port is communicated to cooling device 3 by drainage tube 8,
The cooling device 3 includes closed shell, and inside the shell is filled with coolant;The inside the shell is also provided with cooling by support
Coil pack, coil pack are provided with many cooling tubes 9, and many cooling tubes 9 are sequentially communicated to form roundabout time by elbow two-by-two
Multiple heat exchanger plates 10 are provided with road, and every 9 periphery of cooling tube;The coil pack outlet is connected by straight tube 11
To oily-water seperating equipment 4,4 porch of oily-water seperating equipment is provided with lauter tub, and lauter tub includes tubular support and is laid on tubular
The screen pack of frame outer layer;The oily-water seperating equipment 4 is respectively arranged with wastewater outlet and turpentine oil export.The stirring distillation is anti-
Answer seal closure is provided with the top of tank 1.
The utility model is passed through Oleoresin in retort in processing distillation, then is steamed by 2 pairs of stirrings of electric furnace
Evaporate retort 1 to be heated, while stirring to rosin using stirrer paddle 7, strengthen distilling effect.And in retort
Side is provided with pressure relief opening, drastically raises when air pressure in retort is run into, and can be directly vented by relief valve emergency opening.
Blade is to pull and push connection, easy access.
Again, it is of the present utility model to connect to form roundabout cooling circuit, Ke Yi using elbow using many cooling tubes 9
Largely increase the length of cooling tube 9, strengthen cooling effect.
Meanwhile, the utility model is provided with lauter tub in 4 entrance of oily-water seperating equipment, and lauter tub can be with solid particulate matter and one
The impurity produced in a little production processes is filtered, and carries out periodic cleaning, the blocking in gun barrel.
Preferred embodiment of the present utility model is the foregoing is only, the utility model is not limited to, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all it is of the present utility model spirit and principle
Within, any modification, equivalent substitution and improvements made etc. are should be included within protection domain of the present utility model.
Claims (2)
1. a kind of turpentine oil distills process units, it is characterised in that:Including the stirring distillation reaction tank, cooling dress that are sequentially communicated
Put, oily-water seperating equipment;The stirring distillation reaction pot bottom is provided with heating furnace;It is connected with the stirring distillation reaction tank
Motor, driving motor output shaft are extend in stirring distillation reaction tank, and are connected with axle sleeve, axle sleeve in output shaft upper end
Periphery is provided with multiple bar shaped slots, and in slot is connected with stirrer paddle;At the upper side of the stirring distillation reaction tank
Steam communication port is provided with, and opposite side is provided with pressure relief opening, on pressure relief opening, be connected with blowdown piping, and on blowdown piping
It is connected with relief valve;The steam communication port is communicated to cooling device by drainage tube, and the cooling device includes closed outer
Shell, inside the shell are filled with coolant;The inside the shell is also provided with cooling coil component by support, and coil pack is provided with many
Root cooling tube, many cooling tubes are sequentially communicated to form roundabout loop by elbow two-by-two, and set on every cooling tube periphery
It is equipped with multiple heat exchanger plates;The coil pack outlet is communicated to oily-water seperating equipment, oily-water seperating equipment entrance by straight tube
Place is provided with lauter tub, and lauter tub includes tubular support and is laid on the screen pack of tubular support outer layer;The oily-water seperating equipment point
Wastewater outlet and turpentine oil export are not provided with.
2. turpentine oil according to claim 1 distills process units, it is characterised in that:The stirring distillation reaction tank top
It is provided with seal closure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621024826.2U CN206033660U (en) | 2016-08-31 | 2016-08-31 | Gum spirit distillation apparatus for producing |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201621024826.2U CN206033660U (en) | 2016-08-31 | 2016-08-31 | Gum spirit distillation apparatus for producing |
Publications (1)
Publication Number | Publication Date |
---|---|
CN206033660U true CN206033660U (en) | 2017-03-22 |
Family
ID=58297493
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201621024826.2U Expired - Fee Related CN206033660U (en) | 2016-08-31 | 2016-08-31 | Gum spirit distillation apparatus for producing |
Country Status (1)
Country | Link |
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CN (1) | CN206033660U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861221A (en) * | 2017-04-13 | 2017-06-20 | 惠安县丽佳智能设备有限公司 | A kind of turpentine oil efficiently distills process units |
-
2016
- 2016-08-31 CN CN201621024826.2U patent/CN206033660U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106861221A (en) * | 2017-04-13 | 2017-06-20 | 惠安县丽佳智能设备有限公司 | A kind of turpentine oil efficiently distills process units |
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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: 20170322 Termination date: 20180831 |