CN206033658U - Cryogenic distillation of high -efficient electron production pine fuel economizing device - Google Patents
Cryogenic distillation of high -efficient electron production pine fuel economizing device Download PDFInfo
- Publication number
- CN206033658U CN206033658U CN201621022608.5U CN201621022608U CN206033658U CN 206033658 U CN206033658 U CN 206033658U CN 201621022608 U CN201621022608 U CN 201621022608U CN 206033658 U CN206033658 U CN 206033658U
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- Prior art keywords
- stirring
- cooling
- distillation
- shell
- communicated
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- Expired - Fee Related
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a cryogenic distillation of high -efficient electron production pine fuel economizing device, 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, the driving motor output shaft just is connected with stirring paddle leaf in stretching into stirring distillation reactor jar on the output shaft, and stirring paddle leaf is the streamline form, steam flow hole passes through the drainage tube and communicates cooling device, cooling device includes enclosed housing, and two sets of cooling coil subassemblies about having through the support mounting in the shell, every sleeve disc pipe assembly all are 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 every cooling tube is all built -in to have a refrigeration piece, and the refrigeration piece passes through heat transport ducts and feeds through the heat collecting sheet, and is provided with radiator fan in shell both sides. Adopt the utility model discloses can effectively improve the condensation effect, avoid extravagant.
Description
Technical field
This utility model is related to Colophonium manufacture field, and in particular to a kind of distillation production Oleum Terebinthinae dress of efficient electronic refrigerating
Put.
Background technology
Existing Oleum Terebinthinae 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
This utility model aims to provide a kind of distillation production Oleum Terebinthinae device of efficient electronic refrigerating, to solve above-mentioned asking
Topic.
For achieving the above object, the technical solution of the utility model is as follows：
A kind of distillation production Oleum Terebinthinae device of efficient electronic refrigerating, it is characterised in that：Steam including the stirring being sequentially communicated
Evaporate retort, chiller, oily-water seperating equipment；The stirring distillation reaction pot bottom is provided with heating furnace；The stirring is steamed
Evaporate, driving motor output shaft is extend in stirring distillation reaction tank, and is connected on output shaft
Stirrer paddle is connected to, stirrer paddle is streamline shape；Described stirring is provided with steam communication port at the upper side of distillation reaction tank, and
Opposite side is provided with pressure relief opening, is connected with blowdown piping on pressure relief opening, and is connected with relief valve on blowdown piping；The steam
Communication port is communicated to chiller by drainage tube, and the chiller includes closed shell, and inside the shell is installed by support
There are the two sets of cooling coil components in left and right, often cover coil pack and be provided with many cooling tubes, many cooling tubes pass through elbow two-by-two
It is sequentially communicated to form roundabout loop, and every cooling tube is built-in with cooling piece, cooling piece is communicated to collection by defeated heat pipe
Backing, and shell both sides are provided with radiator fan；The coil pack outlet is communicated to oily-water seperating equipment by straight tube, oil
Water separation device porch is provided with lauter tub, and lauter tub includes tubular support and is laid on the drainage screen of tubular support outer layer；It is described
Oily-water seperating equipment is respectively arranged with wastewater outlet and Lignum Pini Nodi oil export.
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 this utility model
It is interior, then heated to stirring distillation reaction tank by electric furnace, while being stirred to Colophonium 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.
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.And coil pack and right coil pack can be done while making
With increase cooling velocity of liquid assets；Or a set of standby a set of use, strengthen reliability.
Meanwhile, this 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 distillation production Oleum Terebinthinae apparatus structure schematic diagram of the efficient electronic refrigerating that this utility model is provided.
Labelling in figure：1 is stirring distillation reaction tank, 2 is heating furnace, 3 is chiller, 4 is oily-water seperating equipment, 5 are
Motor, 6 be output shaft, 7 be stirrer paddle, 8 be drainage tube, 9 be left coil pack, 10 be right coil pack, 11 be straight
Pipe.
Specific embodiment
This utility model is described further with specific embodiment below in conjunction with the accompanying drawings.
As shown in figure 1, a kind of distillation production Oleum Terebinthinae device of efficient electronic refrigerating, it is characterised in that：Including connecting successively
Logical stirring distillation reaction tank 1, chiller 3, oil-water separation fills 4 and puts；1 bottom of stirring distillation reaction tank is provided with heating
Stove 2；Motor 5 is connected with the stirring distillation reaction tank 1, and 5 output shaft 6 of motor extend into stirring distillation reaction tank
In 1, and stirrer paddle 7 is connected with output shaft 6, stirrer paddle 7 is streamline shape；One above the stirring distillation reaction tank 1
Side is provided with steam communication port, and opposite side is provided with pressure relief opening, is connected with blowdown piping on pressure relief opening, and in blowdown piping
On be connected with relief valve；The steam communication port is communicated to chiller 3 by drainage tube 8, and the chiller 3 includes closing
Formula shell, inside the shell are provided with the two sets of cooling coil components in left and right by support, often cover coil pack and are provided with many coolings
Pipe, many cooling tubes are sequentially communicated to form roundabout loop by elbow two-by-two, and every cooling tube is built-in with cooling piece, system
Cold is communicated to heat collecting sheet by defeated heat pipe, and shell both sides is provided with radiator fan；The coil pack outlet passes through
Straight tube 11 is communicated to oil-water separation and fills 4 to be put, and oil-water separation is filled and is provided with lauter tub at 4 posting ports, and lauter tub includes tubular support and paving
It is located at the drainage screen of tubular support outer layer；The oil-water separation fills 4 puts and is respectively arranged with wastewater outlet and Lignum Pini Nodi oil export.It is described
Seal closure is provided with the top of stirring distillation reaction tank 1.
This 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 Colophonium 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.
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.And coil pack 9 and right coil pack 10 can be done while
Use, increase cooling velocity of liquid assets；Or a set of standby a set of use, strengthen reliability.
Meanwhile, this utility model fills 4 posting ports in oil-water separation and is provided with lauter tub, 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, this utility model is not limited to, for this
For the technical staff in field, this 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 distillation of efficient electronic refrigerating produces Oleum Terebinthinae device, it is characterised in that：Including the stirring distillation being sequentially communicated
Retort, chiller, oily-water seperating equipment；The stirring distillation reaction pot bottom is provided with heating furnace；The stirring distillation
Motor is connected with retort, and driving motor output shaft is extend in stirring distillation reaction tank, and is connected on output shaft
There is stirrer paddle, stirrer paddle is streamline shape；Steam communication port is provided with the upper side of the stirring distillation reaction tank, and another
Side is provided with pressure relief opening, is connected with blowdown piping on pressure relief opening, and is connected with relief valve on blowdown piping；The steam stream
Port is communicated to chiller by drainage tube, and the chiller includes closed shell, and inside the shell is provided with by support
The two sets cooling coil components in left and right, often cover coil pack and are provided with many cooling tubes, many cooling tubes pass through elbow two-by-two according to
Secondary connection forms roundabout loop, and every cooling tube is built-in with cooling piece, and cooling piece is communicated to thermal-arrest by defeated heat pipe
Piece, and shell both sides are provided with radiator fan；The coil pack outlet is communicated to oily-water seperating equipment, profit by straight tube
Segregation apparatuss porch is provided with lauter tub, and lauter tub includes tubular support and is laid on the drainage screen of tubular support outer layer；The oil
Water separation device is respectively arranged with wastewater outlet and Lignum Pini Nodi oil export.
2. the distillation of efficient electronic refrigerating according to claim 1 produces Oleum Terebinthinae device, it is characterised in that：The stirring
Distillation reaction tank top is provided with seal closure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621022608.5U CN206033658U (en) | 2016-08-31 | 2016-08-31 | Cryogenic distillation of high -efficient electron production pine fuel economizing device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621022608.5U CN206033658U (en) | 2016-08-31 | 2016-08-31 | Cryogenic distillation of high -efficient electron production pine fuel economizing device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206033658U true CN206033658U (en) | 2017-03-22 |
Family
ID=58297347
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621022608.5U Expired - Fee Related CN206033658U (en) | 2016-08-31 | 2016-08-31 | Cryogenic distillation of high -efficient electron production pine fuel economizing device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206033658U (en) |
-
2016
- 2016-08-31 CN CN201621022608.5U patent/CN206033658U/en not_active Expired - Fee Related
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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 |
Granted publication date: 20170322 Termination date: 20180831 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |