CN106390502A - High-efficiency turpentine distillation device - Google Patents
High-efficiency turpentine distillation device Download PDFInfo
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- CN106390502A CN106390502A CN201611155910.2A CN201611155910A CN106390502A CN 106390502 A CN106390502 A CN 106390502A CN 201611155910 A CN201611155910 A CN 201611155910A CN 106390502 A CN106390502 A CN 106390502A
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- 238000004821 distillation Methods 0.000 title abstract description 12
- 241000779819 Syncarpia glomulifera Species 0.000 title abstract 6
- 239000001739 pinus spp. Substances 0.000 title abstract 6
- 229940036248 turpentine Drugs 0.000 title abstract 6
- 238000001704 evaporation Methods 0.000 claims abstract description 30
- 238000010438 heat treatment Methods 0.000 claims abstract description 27
- RSWGJHLUYNHPMX-ONCXSQPRSA-N abietic acid Chemical compound C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C(O)=O RSWGJHLUYNHPMX-ONCXSQPRSA-N 0.000 claims description 28
- 238000001816 cooling Methods 0.000 claims description 17
- 239000002826 coolant Substances 0.000 claims description 9
- 239000008601 oleoresin Substances 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 5
- 230000005611 electricity Effects 0.000 claims description 4
- 241000973497 Siphonognathus argyrophanes Species 0.000 claims description 3
- 238000007789 sealing Methods 0.000 claims description 3
- 230000000087 stabilizing effect Effects 0.000 claims description 2
- 240000007594 Oryza sativa Species 0.000 claims 1
- 235000007164 Oryza sativa Nutrition 0.000 claims 1
- 230000004151 fermentation Effects 0.000 claims 1
- 238000000855 fermentation Methods 0.000 claims 1
- 235000009566 rice Nutrition 0.000 claims 1
- 239000007788 liquid Substances 0.000 abstract description 13
- 238000000034 method Methods 0.000 abstract description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 abstract description 2
- 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 abstract description 2
- 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 abstract description 2
- 230000008020 evaporation Effects 0.000 abstract 8
- 239000001293 FEMA 3089 Substances 0.000 abstract 3
- 238000005516 engineering process Methods 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 239000003990 capacitor Substances 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000010355 oscillation Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 235000008331 Pinus X rigitaeda Nutrition 0.000 description 1
- 235000011613 Pinus brutia Nutrition 0.000 description 1
- 241000018646 Pinus brutia Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/12—Molecular distillation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
- C09F1/00—Obtaining purification, or chemical modification of natural resins, e.g. oleo-resins
- C09F1/02—Purification
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09F—NATURAL RESINS; FRENCH POLISH; DRYING-OILS; OIL DRYING AGENTS, i.e. SICCATIVES; TURPENTINE
- C09F3/00—Obtaining spirits of turpentine
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a high-efficiency turpentine distillation device which comprises a molecular evaporation cylinder and a molecular cooler, wherein the molecular evaporation cylinder is shaped like a straight cylinder; a heating jacket is arranged on the cylinder outer wall of the molecular evaporation cylinder; a heating source inlet is formed in the lower part of the heating jacket; a heat source outlet is formed in the upper part of the heating jacket; a connecting flange is arranged at the top of the molecular evaporation cylinder; a vacuum pump interface, a turpentine liquid inlet and a turpentine liquid distribution ring are arranged formed below the connecting flange; a turpentine oil receiving disk, a turpentine oil outlet and a rosin outlet are formed at the bottom of the molecular evaporation cylinder; the inner cylinder wall surface from the turpentine liquid distribution ring to the turpentine oil receiving disk is a molecular evaporation surface; the diameter of the molecular evaporation surface is in the range of 200 mm to 1200 mm; and the vertical length of the molecular evaporation surface is in the range of 1500 mm to 2500 mm. The high-efficiency turpentine distillation device saves the steps of directly evaporating and reducing the distillation temperature and can save energy by more than 70% compared with the distillation method.
Description
Technical field
The present invention relates to a kind of distilling apparatus, specifically a kind of high efficiency Colophonium distilling apparatus.
Background technology
Colophonium is the broad-spectrum raw material of industry.The Colophonium of pinaster contains Colophonium and Oleum Terebinthinae, steams Oleum Terebinthinae and just obtains
Colophonium.Colophonium, through dissolving, supernatant, remove impurity, enters distillation process after being diluted to the fat liquid of good fluidity.In current production technology
Middle distillation fat liquid when have two strands of steam to work, first is indirect steam, and it is conducted heat by coiled pipe, by fat liquid do not stop to heat until
At the end of distillation 195 DEG C about；Second is live (open) steam, and it sprays in fat liquid, extracts Oleum Terebinthinae out with fat liquid mixing azeotropic.This
Technique is referred to as steaming process, is the prevailing technology of current countries in the world Gum Rosin Industry.Though this technique is ripe but energy consumption is big, Colophonium per ton
Consume 1 ton of steam, therefore factory's cauldron, come steam supply, has an impact to environment.In its total energy consumption, dissolving, supernatant twice
Operation accounts for 10% altogether, and distillation process accounts for 90%, in the energy consumption of distillation process, indirect steam account for its 25%, live (open) steam accounts for it
75%.It follows that rosin production will significantly energy-conservation it is necessary to first improve distillation process, first will reduce live (open) steam in a large number,
Second vapo(u)rizing temperature to be reduced, so could obtain obvious energy-saving effect.
Content of the invention
It is an object of the invention to provide a kind of high efficiency Colophonium distilling apparatus, to solve proposition in above-mentioned background technology
Problem.
For achieving the above object, the present invention provides following technical scheme：
A kind of high efficiency Colophonium distilling apparatus, including molecule evaporative cylinder and molecule cooler, described molecule evaporative cylinder is in straight tube
Shape, the drum outer wall of molecule evaporative cylinder has heating jacket, is provided with heating source import in heating jacket bottom, and top is provided with thermal source and goes out
Mouthful, there is adpting flange at molecule evaporative cylinder cylinder top, below adpting flange, have vacuum pump interface, Oleoresin import and Colophonium fat
Liquid histogram ring, has Oleum Terebinthinae flange, Lignum Pini Nodi oil export and Colophonium outlet in molecule evaporative cylinder bottom；In Oleoresin histogram ring extremely
Inner core wall surface between Oleum Terebinthinae flange is molecule evaporating surface, the diameter of the molecule evaporating surface model from 200 millimeters to 1200 millimeters
In enclosing, the vertical length (H) of molecule evaporating surface from 1500 millimeters to 2500 millimeters in the range of；Described molecule cooler is in straight tube
Shape, has adpting flange, the mouth of pipe of coolant inlet pipe and coolant output tube mouth in molecule cooler top planes, and coolant is defeated
Enter the pipe other end and penetrate in molecule cooler, the close dummy seal in molecule cooler bottom；Molecule cooler and molecule evaporative cylinder
Connection be with adpting flange, adpting flange and bolt seal connect, so that molecule cooler is vertically suspended from molecule evaporative cylinder, in
Axis is overlapped with molecule evaporative cylinder axis；The barrel outer surface of molecule cooler is molecule cooling surface, its vertical length with
Molecule evaporating surface equal length；Triangular tooth corrugated arranged vertically is made on molecule cooling surface surface, makes molecule cooling surface
Long-pending expand between 1.5 times to 2 times, the length of side of each triangular tooth ripple is equal, and the length of side is 3 millimeters -6 millimeters, tooth angle is 60 ° -
80 °, tip diameter is less than 20 millimeters to 40 millimeters of molecule evaporating surface diameter, makes between molecule cooling surface and molecule evaporating surface
Distance is between 10 millimeters to 20 millimeters；Described heating source includes rectifier bridge Q, resistance R1, electric capacity C1, electric capacity C5, diode
VD1, potentiometer RP1, when base chip U1 and three terminal regulator U2, described electric capacity C5 one end connect respectively 220V alternating current one end,
Resistance R4 and heating wire RL, the electric capacity C5 other end connects the resistance R4 other end and diode VD4 positive pole respectively, and diode VD4 bears
Pole connects an ac input end of rectifier bridge Q, and it is another that another ac input end of rectifier bridge Q connects 220V alternating current respectively
End and solid-state relay SSR pin 3, described rectifier bridge Q output negative pole connect respectively electric capacity C4, three terminal regulator U1 earth terminal,
Electric capacity C3, resistance R3, electric capacity C2, when base chip U1 pin 1 and electric capacity C1, the electric capacity C4 other end connects rectifier bridge Q output respectively
Positive pole and three terminal regulator U2 input, three terminal regulator U2 outfan connect respectively the electric capacity C3 other end, when base chip U1 draw
Foot 4, when base chip U1 pin 8 and resistance R1, base chip U1 pin 7, diode VD2 negative pole when the resistance R1 other end connects respectively
With diode VD1 positive pole, diode VD1 negative pole connection potentiometer RP1 one end, the potentiometer RP1 other end connects resistance R2, resistance
The R2 other end connect diode VD2 positive pole, potentiometer RP1 slide plate connect respectively the electric capacity C1 other end, when base chip U1 pin 2 and
When base chip U1 pin 6, when base chip U1 pin 3 connecting luminous diode VD3 positive pole, light emitting diode VD3 negative pole connects solid
State relay SSR pin 1, solid-state relay SSR pin 2 connects the resistance R3 other end, and solid-state relay SSR pin 4 connects electricity
The heated filament RL other end.
As the further scheme of the present invention：When described, base chip U1 adopts NE555.
As the further scheme of the present invention：Described three terminal regulator U2 adopts 7805.
As the further scheme of the present invention：Described solid-state relay SSR adopts TAC018.
As the present invention further scheme：Described diode VD4 is Zener diode.
Compared with prior art, the invention has the beneficial effects as follows：The present invention saves live (open) steam and reduces vapo(u)rizing temperature, than
Way of distillation energy-conservation more than 70%.
Brief description
Fig. 1 is the structural representation of high efficiency Colophonium distilling apparatus.
Fig. 2 is the circuit diagram of heating source in high efficiency Colophonium distilling apparatus.
Specific embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation describes.
Refer to Fig. 1～2, in the embodiment of the present invention, a kind of high efficiency Colophonium distilling apparatus, including molecule evaporative cylinder and point
Sub- cooler, described molecule evaporative cylinder is in straight tube shape, and the drum outer wall of molecule evaporative cylinder has heating jacket 8, under heating jacket 8
Portion is provided with heating source import 7, and top is provided with thermal source outlet 9, has adpting flange 15, adpting flange 15 at molecule evaporative cylinder cylinder top
Hereinafter there are vacuum pump interface 10, Oleoresin import 1 and Oleoresin histogram ring 2, have Oleum Terebinthinae to connect in molecule evaporative cylinder bottom
Disk 4, Lignum Pini Nodi oil export 5 and Colophonium outlet 6；Inner core wall surface between Oleoresin histogram ring 2 to Oleum Terebinthinae flange 4 is point
Sub- evaporating surface 3, the diameter D of molecule evaporating surface 3 from 200 millimeters to 1200 millimeters in the range of, the vertical length H of molecule evaporating surface from
In the range of 1500 millimeters to 2500 millimeters；Described molecule cooler is in straight tube shape, has connection in molecule cooler top planes
Flange 11, the mouth of pipe of coolant inlet pipe 12 and coolant output tube mouth 13, it is cold that coolant inlet pipe 12 other end penetrates molecule
But, in device, molecule cooler bottom sealing bottom 16 seals；Molecule cooler is to use adpting flange with the connection of molecule evaporative cylinder
11st, adpting flange 15 and bolt M are tightly connected, and so that molecule cooler is vertically suspended from molecule evaporative cylinder, and axis is steamed with molecule
Send out cylinder axis to overlap；The barrel outer surface of molecule cooler is molecule cooling surface 14, its vertical length and molecule evaporating surface 3
Length H is equal；Triangular tooth corrugated arranged vertically is made on molecule cooling surface 14 surface, so that molecule cooling surface is amassed and expands to
Between 1.5 times to 2 times, length of side C of each triangular tooth ripple is equal, and length of side C is 3 millimeters -6 millimeters, and tooth angle R is 60 ° -80 °, tooth
Outside diameter circle d is less than 20 millimeters to 40 millimeters of molecule evaporating surface 3 diameter, makes between molecule cooling surface 14 and molecule evaporating surface 3
Distance is between 10 millimeters to 20 millimeters；Described heating source includes rectifier bridge Q, resistance R1, electric capacity C1, electric capacity C5, diode
VD1, potentiometer RP1, when base chip U1 and three terminal regulator U2, described electric capacity C5 one end connect respectively 220V alternating current one end,
Resistance R4 and heating wire RL, the electric capacity C5 other end connects the resistance R4 other end and diode VD4 positive pole respectively, and diode VD4 bears
Pole connects an ac input end of rectifier bridge Q, and it is another that another ac input end of rectifier bridge Q connects 220V alternating current respectively
End and solid-state relay SSR pin 3, described rectifier bridge Q output negative pole connect respectively electric capacity C4, three terminal regulator U1 earth terminal,
Electric capacity C3, resistance R3, electric capacity C2, when base chip U1 pin 1 and electric capacity C1, the electric capacity C4 other end connects rectifier bridge Q output respectively
Positive pole and three terminal regulator U2 input, three terminal regulator U2 outfan connect respectively the electric capacity C3 other end, when base chip U1 draw
Foot 4, when base chip U1 pin 8 and resistance R1, base chip U1 pin 7, diode VD2 negative pole when the resistance R1 other end connects respectively
With diode VD1 positive pole, diode VD1 negative pole connection potentiometer RP1 one end, the potentiometer RP1 other end connects resistance R2, resistance
The R2 other end connect diode VD2 positive pole, potentiometer RP1 slide plate connect respectively the electric capacity C1 other end, when base chip U1 pin 2 and
When base chip U1 pin 6, when base chip U1 pin 3 connecting luminous diode VD3 positive pole, light emitting diode VD3 negative pole connects solid
State relay SSR pin 1, solid-state relay SSR pin 2 connects the resistance R3 other end, and solid-state relay SSR pin 4 connects electricity
The heated filament RL other end.When described, base chip U1 adopts NE555.Described three terminal regulator U2 adopts 7805.Described solid-state relay
SSR adopts TAC018.Described diode VD4 is Zener diode.
Undulatory for triangular tooth cooling surface tip diameter is made less than the diameter of molecule evaporating surface by apparatus of the present invention
20 millimeters to 40 millimeters, make the distance between molecule cooling surface and molecule evaporating surface between 10 millimeters to 20 millimeters, be basis
Molecular motion principle, when fat liquid film flows through molecule evaporating surface in condition of high vacuum degree, the Colophonium molecule in fat liquid film and Lignum Pini Nodi oil
Son all can make molecular motion by respective moving radius when heated, constantly from the effusion of fat liquid film face and return.Due to Oleum Terebinthinae
Boiling point is more much lower than Colophonium, and the distance of its molecular motion under the same conditions is far more a lot of than Colophonium molecule, so this Colophonium short distance
Distillator molecule cooling surface is located at during Oleum Terebinthinae molecular motion and can reach and Colophonium molecule is unable in reach, i.e. molecule
The distance between cooling surface and molecule evaporating surface differ 10 millimeters to 20 millimeters, and such molecule cooling surface just can catch and cool down pine
Fuel-economizing molecule, and Colophonium molecule then returns fat liquid film.
Heating source adopts optical electrical formula solid-state relay SSR, and control circuit and heating wire RL are carried out electrical isolation, safety
Reliable, its another feature be heat time heating time can according to temperature rise need voluntarily adjust, easy to adjust.Circuit is by step-down rectifier
The adjustable multivibrator of circuit, dutycycle（It is made up of NE555）Form with solid-state relay SSR control circuit etc..
Step-down rectifying circuit is made up of decompression capacitor C5, rectifier bridge Q and filter capacitor C4, and through three terminal regulator U2
（7809）Voltage stabilizing goes out+9V voltage, is that control circuit is powered, control heat up heater circuit be with when base chip NE555 as core
Composition, NE555 and R1, the adjustable LF multivibrator of R2, RP1, VD1, VD2 one dutycycle of composition, its cycle of oscillation
It is a definite value, but dutycycle can be adjusted by RP1.
Under conditions of cycle of oscillation is constant, by adjusting RP1, can change electricity in interior its dutycycle of change on a large scale
The heat-up periods time of heated filament RL（The on/off time）.Between NE555 output high period, VD3 lights（Represent and heat）, and
It is added to the primary of optical electrical formula solid-state relay SSR, coupled by optical electrical, the IGBT group through SSR level of solid-state relay
Conducting, heats heating wire RL electrified regulation, and heating wire heats up, and after temperature rise reaches temperature required, by adjusting RP1, makes duty
Ratio reduction, keeps heating wire temperature constant.
It is obvious to a person skilled in the art that the invention is not restricted to the details of above-mentioned one exemplary embodiment, Er Qie
In the case of the spirit or essential attributes of the present invention, the present invention can be realized in other specific forms.Therefore, no matter
From the point of view of which point, embodiment all should be regarded as exemplary, and be nonrestrictive, the scope of the present invention is by appended power
Profit requires rather than described above limits, it is intended that all in the implication and scope of the equivalency of claim by falling
Change is included in the present invention.Any reference in claim should not be considered as limiting involved claim.
Moreover, it will be appreciated that although this specification is been described by according to embodiment, not each embodiment only wraps
Containing an independent technical scheme, only for clarity, those skilled in the art should for this narrating mode of description
Using description as an entirety, the technical scheme in each embodiment can also form those skilled in the art through appropriately combined
Understandable other embodiment.
Claims (5)
1. a kind of high efficiency Colophonium distilling apparatus, including molecule evaporative cylinder and molecule cooler it is characterised in that described molecule
Evaporative cylinder is in straight tube shape, and the drum outer wall of molecule evaporative cylinder has heating jacket (8), is provided with heating source in heating jacket (8) bottom and enters
Mouth (7), top is provided with thermal source outlet (9), has adpting flange (15) at molecule evaporative cylinder cylinder top, has below adpting flange (15)
Vacuum pump interface (10), Oleoresin import (1) and Oleoresin histogram ring (2), have Oleum Terebinthinae to connect in molecule evaporative cylinder bottom
Disk (4), Lignum Pini Nodi oil export (5) and Colophonium outlet (6)；Inner core between Oleoresin histogram ring (2) to Oleum Terebinthinae flange (4)
Wall surface is molecule evaporating surface (3), the diameter (D) of molecule evaporating surface (3) from 200 millimeters to 1200 millimeters in the range of, molecule steams
Fermentation vertical length (H) from 1500 millimeters to 2500 millimeters in the range of；Described molecule cooler is in straight tube shape, cold in molecule
But device top planes have adpting flange (11), the mouth of pipe of coolant inlet pipe (12) and coolant output tube mouth (13), coolant
Input pipe (12) other end penetrates in molecule cooler, sealing bottom (16) sealing of molecule cooler bottom；Molecule cooler with
The connection of molecule evaporative cylinder is to be tightly connected with adpting flange (11), adpting flange (15) and bolt (M), so that molecule cooler is hung down
Directly it is suspended from molecule evaporative cylinder, axis is overlapped with molecule evaporative cylinder axis；The barrel outer surface of molecule cooler is molecule
Cooling surface (14), its vertical length is equal with molecule evaporating surface (3) length (H)；Molecule cooling surface (14) surface is made vertically
The triangular tooth corrugated of arrangement, makes molecule cooling surface amass and expands between 1.5 times to 2 times, the side of each triangular tooth ripple
Long (C) is equal, and the length of side (C) is 3 millimeters -6 millimeters, and tooth angle (R) is 60 ° -80 °, and tip diameter (d) is less than molecule evaporating surface
(3) 20 millimeters to 40 millimeters of diameter, make the distance between molecule cooling surface (14) and molecule evaporating surface (3) at 10 millimeters to 20 millis
Between rice；Described heating source includes rectifier bridge Q, resistance R1, electric capacity C1, electric capacity C5, diode VD1, potentiometer RP1, Shi Jixin
Piece U1 and three terminal regulator U2, described electric capacity C5 one end connects 220V alternating current one end, resistance R4 and heating wire RL, electric capacity respectively
The C5 other end connects the resistance R4 other end and diode VD4 positive pole respectively, and diode VD4 negative pole connects a friendship of rectifier bridge Q
Stream input, another ac input end of rectifier bridge Q connects the 220V alternating current other end and solid-state relay SSR pin respectively
3, described rectifier bridge Q output negative pole connect respectively electric capacity C4, three terminal regulator U1 earth terminal, electric capacity C3, resistance R3, electric capacity C2,
When base chip U1 pin 1 and electric capacity C1, the electric capacity C4 other end connects rectifier bridge Q output cathode and three terminal regulator U2 input respectively
End, three terminal regulator U2 outfan connect respectively the electric capacity C3 other end, when base chip U1 pin 4, when base chip U1 pin 8 and electricity
Resistance R1, base chip U1 pin 7, diode VD2 negative pole and diode VD1 positive pole, diode when the resistance R1 other end connects respectively
VD1 negative pole connects potentiometer RP1 one end, and the potentiometer RP1 other end connects resistance R2, and the resistance R2 other end connects diode VD2
Positive pole, potentiometer RP1 slide plate connect respectively the electric capacity C1 other end, when base chip U1 pin 2 and Shi Ji chip U1 pin 6, Shi Ji
Chip U1 pin 3 connecting luminous diode VD3 positive pole, light emitting diode VD3 negative pole connects solid-state relay SSR pin 1, solid-state
Relay SSR pin 2 connects the resistance R3 other end, and solid-state relay SSR pin 4 connects the heating wire RL other end.
2. high efficiency Colophonium distilling apparatus according to claim 1 it is characterised in that when described base chip U1 adopt
NE555.
3. high efficiency Colophonium distilling apparatus according to claim 1 are it is characterised in that described three terminal regulator U2 adopts
7805.
4. high efficiency Colophonium distilling apparatus according to claim 1 are it is characterised in that described solid-state relay SSR adopts
TAC018.
5. high efficiency Colophonium distilling apparatus according to claim 1 are it is characterised in that described diode VD4 is voltage stabilizing two
Pole pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611155910.2A CN106390502A (en) | 2016-12-14 | 2016-12-14 | High-efficiency turpentine distillation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611155910.2A CN106390502A (en) | 2016-12-14 | 2016-12-14 | High-efficiency turpentine distillation device |
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| Publication Number | Publication Date |
|---|---|
| CN106390502A true CN106390502A (en) | 2017-02-15 |
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ID=58087763
Family Applications (1)
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| CN201611155910.2A Pending CN106390502A (en) | 2016-12-14 | 2016-12-14 | High-efficiency turpentine distillation device |
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Cited By (1)
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| CN106975236A (en) * | 2017-04-28 | 2017-07-25 | 南宁市青秀区嘉利林化有限公司 | A kind of rosin vacuum distillation apparatus |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106975236A (en) * | 2017-04-28 | 2017-07-25 | 南宁市青秀区嘉利林化有限公司 | A kind of rosin vacuum distillation apparatus |
| CN106975236B (en) * | 2017-04-28 | 2019-10-22 | 广西南宁成远科技有限公司 | A kind of rosin vacuum distillation apparatus |
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Application publication date: 20170215 |
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