CN206167961U - Distillation and condensation device - Google Patents
Distillation and condensation device Download PDFInfo
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- CN206167961U CN206167961U CN201621182055.XU CN201621182055U CN206167961U CN 206167961 U CN206167961 U CN 206167961U CN 201621182055 U CN201621182055 U CN 201621182055U CN 206167961 U CN206167961 U CN 206167961U
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- condensing unit
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Abstract
The utility model discloses a distillation and condensation device, its technical scheme main points are: including raw material vat and to the constant temperature bath pot of raw material vat heating, the raw material vat intercommunication has condensing assembly, has stretched into the rabbling mechanism in the raw material vat, and the rabbling mechanism includes the drive assembly of blade subassembly, (mixing) shaft and drive (mixing) shaft, and the blade subassembly is fixed on the (mixing) shaft, and drive assembly includes motor and cylinder, the output shaft (mixing) shaft of motor, and the motor is fixed on the flat board, the piston rod and the dull and stereotyped one side fixed connection who keeps away from the motor of cylinder, the cylinder is fixed on the support, the utility model has the advantages that the rabbling mechanism can rotate the stirring simultaneously and mix from top to bottom for the stirring is more abundant during the distillation, accelerates the distillation speed.
Description
Technical field
The utility model is related to distillation condensing plant field, and in particular to one kind distillation condensing unit.
Background technology
Distillation condensing plant is frequently utilized for chemical extraction reaction, pharmacy, brews alcoholic beverages etc. field, to be heated by raw material,
The organic matter in raw material is vaporized, and is extracted by condensing to liquefy organic matter.
Existing distillation condensing unit usually stretches into agitating shaft in reactor, and raw material is stirred in heating, with
Reactant is set to be heated more fully, so as to accelerate the evaporation of organic matter.Chinese patent such as Publication No. CN103239881A is public
A kind of distilling apparatus, including fluid reservoir are opened, charge door has been provided with the top of fluid reservoir and evacuation port, bottom is provided with discharging
Mouthful, it is looped around reservoir exterior surface and is provided with heating pipe, the rabbling mechanism of fluid reservoir also is inserted from the top vertical of fluid reservoir,
Rabbling mechanism includes successively from top to bottom：The agitator arm of reductor and the reductor connection of motor and motor connection, it is arranged on
Agitation blade on agitator arm.Drive rabbling mechanism to be stirred the liquid in fluid reservoir by motor, make heated liquid more
Plus fully, accelerate the distillation speed of liquid.
Although the stirring mechanism includes three-stage type agitation blades, the agitation blade can only rotate, it is impossible to drive liquid
Stirred up and down, if it is desired to which stirring is more abundant, in addition it is also necessary to which design one kind stirs more fully device up and down.
Utility model content
The purpose of this utility model is to provide a kind of distillation condensing unit, and its advantage is that rabbling mechanism can be stirred while rotating
Mix and stir and stir up and down so that stirring more fully, accelerates distillation speed during distillation.
Above-mentioned technical purpose of the present utility model technical scheme is that：One kind distillation condensation dress
Put, including raw cylinder and the constant temperature bath to raw cylinder heating, the raw cylinder is communicated with condensation, in the raw cylinder
Rabbling mechanism is stretched into, the rabbling mechanism includes blade assembly, agitating shaft and drives the drive component of the agitating shaft, described
Blade assembly is fixed on the agitating shaft, and the drive component includes motor and cylinder, the output shaft connection institute of the motor
Agitating shaft is stated, the motor is fixed on flat board, the piston rod of the cylinder is fixed away from the one side of motor with the flat board and connected
Connect, the cylinder is fixed on support.
By above-mentioned technical proposal, cylinder is moved up and down by the telescopic drive flat board of piston rod, and drive motor is gone up together
Lower motion, the output shaft of motor drives agitating shaft to be rotated, and the movement locus of blade assembly is the conjunction of rotation and linear motion
Motion, is stirred so that the raw material in raw cylinder is sufficiently agitated up and down while Stirring, reaches preferably stirring
Effect.
The utility model is further arranged to：The support includes vertical stand and level frame, and the cylinder is fixed on described
On level frame, the level frame two ends are equipped with sliding block, and the sliding block is slidably connected with the vertical stand.
By above-mentioned technical proposal, vertical stand is fixed on the surrounding of raw cylinder, and level frame two ends pass through sliding block and erect respectively
Straight frame is slidably connected, and cylinder is fixed in the middle of level frame, and piston rod is set down, can be adjusted by adjusting the height of level frame
The distance of displacements of cylinders relative raw material cylinder, adjusts agitating shaft and stretches into raw cylinder such that it is able to the depth according to raw material in raw cylinder
Depth so that the stroke of cylinder piston rod can reach the purpose being sufficiently stirred for raw material, it is ensured that mixing effect.
The utility model is further arranged to：The blade assembly includes straight leaf formula stirring vane and pusher paddle
Piece, the pusher stirring vane is helical form.
By above-mentioned technical proposal, straight leaf formula stirring vane is each attached on agitating shaft with pusher stirring vane, straight leaf
Formula stirring vane be used for stir raw material liq rotation, pusher stirring vane stir raw material rotate while, because it is spiral shell
Revolve shape to set, therefore raw material can be stirred with the vertical direction, two kinds of stirring vanes are stirred simultaneously so that it is same that raw material rotates
When stirred up and down, therefore be stirred more abundant.
The utility model is further arranged to：The condensation includes jet chimney, ball-type bottle and condenser pipe, the steaming
Steam pipe road one end connects with the raw cylinder, and the jet chimney other end is connected with ball-type bottle side, the ball-type
Bottle upper end is connected with the condenser pipe, and the ball-type bottle lower end is provided with leakage fluid dram, and the leakage fluid dram is provided with tapping valve.
By above-mentioned technical proposal, the steam distilled out in raw cylinder enters in condenser pipe from jet chimney, condenses to the cold
After liquefy, be dropped in below condenser pipe ball-type bottle in, open tapping valve, you can by liquid from leakage fluid dram take out.
The utility model is further arranged to：The vertical axis of the relatively described ball-type bottle of the jet chimney are vertically arranged.
By above-mentioned technical proposal, if jet chimney is inclined with respect to the vertical axis of ball-type bottle, it is unfavorable on steam
Rise and enter in condenser pipe, or the liquid being easily caused in ball-type bottle flows back into jet chimney；Therefore jet chimney needs phase
Vertical axis to ball-type bottle are vertically arranged, i.e., jet chimney keeps level.
The utility model is further arranged to：The condenser pipe is communicated with pump-line, and the pump-line is connected with to be taken out
Air pump.
By above-mentioned technical proposal, aspiration pump, to being evacuated in equipment, reduces the pressure in raw cylinder by pump-line
By force, because the boiling point of liquid is reduced as pressure reduces, pressure reduces in raw cylinder, the boiling point reduction of raw material, in distillation
It is more prone to evaporation, distilling effect is more preferable.
The utility model is further arranged to：Also include stretching into the thermometer in the raw cylinder.
By above-mentioned technical proposal, thermometer can detect the real time temperature in raw cylinder, be conducive to operating personnel to observe
With the heating state judged in raw cylinder, and heating-up temperature is therefore adjusted, make the process temperature of distillation more accurate suitable.
The utility model is further arranged to：The raw cylinder is provided with auxiliary inlet.
By above-mentioned technical proposal, auxiliary inlet is used for when needed to adding liquid material in raw cylinder, using drop
Pipe stretches into auxiliary inlet and is added dropwise.
The utility model is further arranged to：The raw cylinder is provided with sample tap.
By above-mentioned technical proposal, sample tap is used to be sampled the raw material in raw cylinder, to detect the state of raw material.
In sum, the utility model has the advantages that：
1st, blade assembly is stirred up and down while Stirring, and is arranged to straight leaf formula stirring vane and is stirred with push type
Mix the combination type vane of blade one so that whipping process becomes abundant, mixing effect more preferably, is advantageously carried out in raw material
Distillation；
2nd, aspiration pump is evacuated by pump-line to equipment, reduces the pressure in raw cylinder, and pressure subtracts in raw cylinder
Small, the boiling point reduction of raw material is more prone to evaporation in distillation, and distilling effect is more preferable.
Brief description of the drawings
Fig. 1 is the structural representation of embodiment 1；
Fig. 2 is the schematic diagram of embodiment sliding block and bolt arrangement in embodiment 1；
Fig. 3 is the schematic diagram of embodiment rabbling mechanism structure in embodiment 1；
Fig. 4 is the schematic diagram of embodiment condenser tube structure in embodiment 1；
Fig. 5 is the structural representation of embodiment 2；
Fig. 6 is the structural representation of embodiment 3.
In figure, 1, raw cylinder；11st, drain hole；12nd, inlet is aided in；13rd, sample tap；14th, stopper；15th, thermometer；2、
Casing；21st, constant temperature bath；3rd, rabbling mechanism；31st, drive component；311st, motor；3111st, output shaft；312nd, cylinder；32nd, stir
Axle；321st, blade assembly；3211st, straight leaf formula stirring vane；3212nd, pusher stirring vane；33rd, flat board；331st, shaft coupling；
34th, support；341st, vertical stand；342nd, level frame；3421st, sliding block；3422nd, bolt；4th, jet chimney；5th, ball-type bottle；51st, discharge opeing
Mouthful；511st, tapping valve；6th, condenser pipe；61st, fixed mount；62nd, condensing water conduit；621st, water inlet；622nd, delivery port；7th, exhaust tube
Road；71st, aspiration pump.
Specific embodiment
The utility model is described in further detail below in conjunction with accompanying drawing.
Embodiment 1：One kind distillation condensing unit, as shown in figure 1, including raw cylinder 1, raw cylinder 1 is placed on constant temperature bath
In 21, after adding raw material from the drain hole 11 of raw cylinder 1, using the heat transfer water in constant temperature bath 21 to raw cylinder 1, to raw cylinder
Raw material in 1 carries out heating distillation.
As depicted in figs. 1 and 2, the casing 2 of constant temperature bath 21 is fixedly arranged above support 34, and support 34 includes level frame 342
With vertical stand 341, vertical stand 341 is fixed on the casing 2 of constant temperature bath 21, and the two ends of level frame 342 are fixed with sliding block 3421,
Sliding block 3421 is set in vertical stand 341, in the enterprising line slip of vertical stand 341, and can be fixed by bolt 3422.
As shown in figures 1 and 3, it is fixed with cylinder 312 in the middle of level frame 342, the original of the piston rod of cylinder 312 lower section down
Material cylinder 1, piston rod is fixed with flat board 33 away from one end of cylinder 312, and flat board 33 is fixed with motor away from one end of piston rod
311, the output shaft 3111 of motor 311 is connected with agitating shaft 32 by shaft coupling 331, and agitating shaft 32 is stretched into raw cylinder 1, passed through
Fixed blade assembly 321 is stirred to raw material on agitating shaft 32.
Cylinder 312 is moved up and down by the telescopic drive flat board 33 of piston rod, and drive motor 311 moves up and down together, electricity
The output shaft 3111 of machine 311 drives agitating shaft 32 to be rotated, and the movement locus of blade assembly 321 is rotation and linear motion
Resultant motion, is stirred up and down while Stirring so that the raw material in raw cylinder 1 is sufficiently agitated, and is reached preferably
Mixing effect.
The distance of the relative raw material cylinder 1 of cylinder 312 can be adjusted by adjusting the height of level frame 342, such that it is able to root
The depth that agitating shaft 32 is stretched into raw cylinder 1 is adjusted according to the depth of raw material in raw cylinder 1 so that the row of the piston rod of cylinder 312
Journey can reach the purpose being sufficiently stirred for raw material, it is ensured that mixing effect.
Blade assembly 321 includes straight leaf formula stirring vane 3211 and spiral helicine pusher stirring vane 3212, straight leaf formula
Stirring vane 3211 is located at the bottom of agitating shaft 32, and pusher stirring vane 3212 is located at the upper of straight leaf formula stirring vane 3211
Side.Straight leaf formula stirring vane 3211 is each attached on agitating shaft 32 with pusher stirring vane 3212, straight leaf formula stirring vane
3211 be used for stir raw material liq rotation, pusher stirring vane 3212 stir raw material rotate while, because it is spiral
Shape is set, therefore can stir raw material with the vertical direction, and two kinds of stirring vanes are stirred simultaneously so that while raw material rotates
Stirred up and down, therefore be stirred more abundant, so as to distill more abundant.
As shown in figure 1, being additionally provided with auxiliary inlet 12 on raw cylinder 1, and be provided with sample tap 13, auxiliary inlet 12 with
Sample tap 13 is clogged by stopper 14.Auxiliary inlet 12 is stretched into using dropper when needed, to adding liquid in raw cylinder 1
Material.Sample tap 13 is used to be sampled the raw material in raw cylinder 1, to detect the state of raw material.
As shown in Figure 1 and Figure 4, raw cylinder 1 is communicated with jet chimney 4, and jet chimney 4 is communicated with ball-type bottle 5, ball-type bottle 5
It is vertically arranged, jet chimney 4 is vertical with respect to the vertical axis of ball-type bottle 5, and jet chimney 4 keeps horizontally disposed.5 upper ends of ball-type bottle
Condenser pipe 6 is connected with, condenser pipe 6 is vertically arranged, and is fixed by fixed mount 61, is fixed with condenser pipe 6 spiral helicine
Condensing water conduit 62, external condensed water enters in condenser pipe 6 from the water inlet 621 of condensing water conduit 62, and from condensate pipe
The delivery port 622 in road 62 flows out.
Leakage fluid dram 51 is provided with 5 lower ends of ball-type bottle, leakage fluid dram 51 is provided with tapping valve 511, the steam condensation in condenser pipe 6
After be dropped in ball-type bottle 5, and taken out from leakage fluid dram 51.
Embodiment 2：One kind distillation condensing unit, the difference with embodiment 1 is, as shown in figure 5, the table of raw cylinder 1
Face is also inserted with thermometer 15, and thermometer 15 is stretched into raw cylinder 1, can detect the real time temperature in raw cylinder 1, is conducive to operation
Personal observations and judge the heating state in raw cylinder 1, and therefore adjust heating-up temperature, make the process temperature of distillation more accurate
Properly.
Embodiment 3：One kind distillation condensing unit, the difference with embodiment 2 is, as shown in fig. 6, on condenser pipe 6
End is communicated with pump-line 7, and pump-line 7 is connected with aspiration pump 71.Aspiration pump 71 is taken out by pump-line 7 to equipment
Gas, reduces the pressure in raw cylinder 1, because the boiling point of liquid is reduced as pressure reduces, pressure reduces in raw cylinder 1, former
The boiling point reduction of material, evaporation is more prone in distillation, and distilling effect is more preferable.
The course of work：The course of work is illustrated with reference to above-mentioned all embodiments, the reality of each of which separate embodiments
The mode of applying is all contained in the middle of this implementation process.Raw material is added from the drain hole 11 of raw cylinder 1 first, according to raw material in raw cylinder
Depth in 1, adjusts the height of level frame 342, agitating shaft 32 is fully stretched into raw material, and raw material is entered using constant temperature bath 21
Row heating distillation.Start motor 311 and cylinder 312 simultaneously, cylinder 312 drives agitating shaft to be stirred about 32, and motor 311 drives and stirs
Axle 32 is mixed to be rotated；Start aspiration pump 71 to being evacuated to reduce pressure in equipment, reduce the boiling point of liquid；In raw material
Organic matter receives thermal evaporation, and steam is entered in condenser pipe 6 by jet chimney 4, condensed to the cold, becomes liquid and is dropped in ball-type bottle 5
It is interior, and taken out from leakage fluid dram 51.
The utility model Stirring and can be stirred up and down simultaneously so that stirring more fully, is accelerated to distill during distillation
Speed.
This specific embodiment is only that, to explanation of the present utility model, it is not to limitation of the present utility model, ability
Field technique personnel can make the modification without creative contribution to the present embodiment as needed after this specification is read, but
As long as all being protected by Patent Law in right of the present utility model.
Claims (9)
1. a kind of distillation condensing unit, including raw cylinder（1）And to raw cylinder（1）The constant temperature bath of heating（21）, the original
Material cylinder（1）It is communicated with condensation, the raw cylinder（1）Rabbling mechanism is inside stretched into（3）, it is characterized in that：The rabbling mechanism
（3）Including blade assembly（321）, agitating shaft（32）With the driving agitating shaft（32）Drive component（31）, the blade group
Part（321）It is fixed on the agitating shaft（32）On, the drive component（31）Including motor（311）And cylinder（312）, the electricity
Machine（311）Output shaft（3111）Connect the agitating shaft（32）, the motor（311）It is fixed on flat board（33）On, the gas
Cylinder（312）Piston rod and the flat board（33）Away from motor（311）One side be fixedly connected, the cylinder（312）It is fixed on
Support（34）On.
2. one kind according to claim 1 distills condensing unit, it is characterized in that：The support（34）Including vertical stand
（341）And level frame（342）, the cylinder（312）It is fixed on the level frame（342）On, the level frame（342）Two ends are equal
It is provided with sliding block（3421）, the sliding block（3421）With the vertical stand（341）It is slidably connected.
3. one kind according to claim 1 distills condensing unit, it is characterized in that：The blade assembly（321）Including straight leaf
Formula stirring vane（3211）With pusher stirring vane（3212）, the pusher stirring vane（3212）It is helical form.
4. one kind according to claim 1 distills condensing unit, it is characterized in that：The condensation includes jet chimney
（4）, ball-type bottle（5）And condenser pipe（6）, the jet chimney（4）One end and the raw cylinder（1）Connection, the jet chimney
（4）The other end and ball-type bottle（5）Side is connected, the ball-type bottle（5）Upper end and the condenser pipe（6）It is connected, institute
State ball-type bottle（5）Lower end is provided with leakage fluid dram（51）, the leakage fluid dram（51）It is provided with tapping valve（511）.
5. one kind according to claim 4 distills condensing unit, it is characterized in that：The jet chimney（4）Relatively described ball
Type bottle（5）Vertical axis be vertically arranged.
6. one kind according to claim 4 distills condensing unit, it is characterized in that：The condenser pipe（6）It is communicated with exhaust tube
Road（7）, the pump-line（7）It is connected with aspiration pump（71）.
7. one kind according to claim 1 distills condensing unit, it is characterized in that：Also include stretching into the raw cylinder（1）It is interior
Thermometer（15）.
8. one kind according to claim 1 distills condensing unit, it is characterized in that：The raw cylinder（1）Be provided with aid in into
Liquid mouthful（12）.
9. one kind according to claim 1 distills condensing unit, it is characterized in that：The raw cylinder（1）It is provided with sample tap
（13）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621182055.XU CN206167961U (en) | 2016-11-03 | 2016-11-03 | Distillation and condensation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621182055.XU CN206167961U (en) | 2016-11-03 | 2016-11-03 | Distillation and condensation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206167961U true CN206167961U (en) | 2017-05-17 |
Family
ID=58681845
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621182055.XU Expired - Fee Related CN206167961U (en) | 2016-11-03 | 2016-11-03 | Distillation and condensation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206167961U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108192795A (en) * | 2018-01-15 | 2018-06-22 | 沈墅 | A kind of tower gas-liquid binary states alcohol distillation extracting system |
| CN108192794A (en) * | 2018-01-15 | 2018-06-22 | 沈墅 | A kind of list using energy source formula alcohol distillation extracting system |
| CN108660049A (en) * | 2018-06-29 | 2018-10-16 | 贵州省仁怀市茅台镇永泰酒业股份有限公司 | A kind of wine brewing distilling apparatus |
| CN117180773A (en) * | 2023-09-08 | 2023-12-08 | 海能未来技术集团股份有限公司 | Kai's distillation system and method for automatically connecting and separating digestion tubes in static state |
-
2016
- 2016-11-03 CN CN201621182055.XU patent/CN206167961U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108192795A (en) * | 2018-01-15 | 2018-06-22 | 沈墅 | A kind of tower gas-liquid binary states alcohol distillation extracting system |
| CN108192794A (en) * | 2018-01-15 | 2018-06-22 | 沈墅 | A kind of list using energy source formula alcohol distillation extracting system |
| CN108192794B (en) * | 2018-01-15 | 2021-08-13 | 沈墅 | Single-energy-source utilization type alcohol distillation extraction system |
| CN108192795B (en) * | 2018-01-15 | 2021-08-13 | 沈墅 | Tower-type gas-liquid two-state alcohol distillation and extraction system |
| CN108660049A (en) * | 2018-06-29 | 2018-10-16 | 贵州省仁怀市茅台镇永泰酒业股份有限公司 | A kind of wine brewing distilling apparatus |
| CN117180773A (en) * | 2023-09-08 | 2023-12-08 | 海能未来技术集团股份有限公司 | Kai's distillation system and method for automatically connecting and separating digestion tubes in static state |
| CN117180773B (en) * | 2023-09-08 | 2024-02-13 | 海能未来技术集团股份有限公司 | Kai's distillation system and method for automatically connecting and separating digestion tubes in static state |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170517 Termination date: 20201103 |
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| CF01 | Termination of patent right due to non-payment of annual fee |