CN217651177U - Distiller for liquor production - Google Patents
Distiller for liquor production Download PDFInfo
- Publication number
- CN217651177U CN217651177U CN202123341930.8U CN202123341930U CN217651177U CN 217651177 U CN217651177 U CN 217651177U CN 202123341930 U CN202123341930 U CN 202123341930U CN 217651177 U CN217651177 U CN 217651177U
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- Prior art keywords
- pipe
- heating furnace
- fixed
- distillation
- linked together
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- Expired - Fee Related
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 238000010438 heat treatment Methods 0.000 claims abstract description 38
- 238000004821 distillation Methods 0.000 claims abstract description 35
- 239000007788 liquid Substances 0.000 claims abstract description 35
- 238000001816 cooling Methods 0.000 claims abstract description 25
- 238000000746 purification Methods 0.000 claims abstract description 19
- 239000003517 fume Substances 0.000 claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 238000001179 sorption measurement Methods 0.000 claims description 10
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 11
- 239000003546 flue gas Substances 0.000 abstract description 11
- 238000007599 discharging Methods 0.000 abstract description 6
- 239000000779 smoke Substances 0.000 description 12
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000012535 impurity Substances 0.000 description 7
- 239000003595 mist Substances 0.000 description 7
- 239000000110 cooling liquid Substances 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 230000002035 prolonged effect Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000010977 unit operation Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a distiller for white spirit production, including heating furnace, distillation barrel, cooling tank, distillation tube and purifying box, the distillation barrel is installed on the top of heating furnace, and the top of distillation barrel is fixed with the distillation tube, and the distillation tube is linked together with the distillation barrel to be fixed with the pipe of discharging fume on the outer wall at heating furnace top, the pipe of discharging fume is linked together with the heating furnace, one side of heating furnace is provided with the purifying box, and the purifying box is linked together with the pipe of discharging fume, the opposite side of heating furnace is provided with the liquid storage pot, and the top of liquid storage pot is fixed with the cooling tank, and the cooling tank is linked together with the liquid storage pot, the inside of cooling tank is provided with the spiral pipe, and the top of spiral pipe is fixed with the connecting pipe, one side that the heating furnace was kept away from to the liquid storage pot is provided with the collecting vessel. The utility model discloses not only improve the utilization ratio to the fog, be convenient for carry out purification treatment to the flue gas, moreover the effectual pollution that the distillate received that has reduced.
Description
Technical Field
The utility model relates to a white spirit production technical field specifically is a distiller for white spirit production.
Background
The distillation is a thermodynamic separation process, it utilizes the different boiling points of every component in the mixed liquid or liquid-solid system, make the low boiling point component evaporate, condense in order to separate the unit operation process of the whole component, it is the union of two kinds of unit operations of evaporation and condensation, compared with other separation means, such as extraction and filtering crystallization, etc., its advantage lies in not needing to use other solvents besides system's component, thus guarantee will not introduce new impurity, because the production of white spirit mostly adopts the way of distillation, therefore need to finish with the aid of the distiller.
The types of the distillers on the market are various, and can basically meet the use requirements of people, but certain defects still exist, and the specific problems are as follows.
(1) The gas-liquid conversion rate of the existing distiller is low when the distiller is used, so that the utilization rate of mist is general;
(2) The existing distiller is inconvenient to purify flue gas generated by combustion when in use, and is easy to cause atmospheric pollution when directly discharged;
(3) The existing distiller is generally in an open material receiving mode when in use, so that distillate is easy to be polluted when being discharged, and thus, the improvement space exists.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a distiller for white spirit production to it remains to improve to solve the gas-liquid conversion rate when using to provide the distiller in the above-mentioned background art, and the problem that receives the pollution easily when carrying out purification treatment and distillate discharge to the flue gas that the burning produced is inconvenient.
In order to achieve the above purpose, the utility model provides a following technical scheme: the utility model provides a distiller for white spirit production, includes heating furnace, retort, cooling tank, distillation tube and purifying box, the retort is installed on the top of heating furnace, and the top of retort is fixed with the distillation tube, and the distillation tube is linked together with the retort to be fixed with the pipe of discharging fume on the outer wall at heating furnace top, the pipe of discharging fume is linked together with the heating furnace, one side of heating furnace is provided with the purifying box, and the purifying box is linked together with the pipe of discharging fume, the opposite side of heating furnace is provided with the liquid storage pot, and the top of liquid storage pot is fixed with the cooling tank, and the cooling tank is linked together with the liquid storage pot, one side that the heating furnace was kept away from to the liquid storage pot is provided with the collecting tank.
Preferably, the inside of cooling tank is provided with the spiral pipe, and the top of spiral pipe is fixed with the connecting pipe, and the top of connecting pipe is linked together with the bottom of distillation tube, has prolonged the contact time of fog and coolant liquid for gas-liquid conversion is more abundant, and conversion efficiency is higher.
Preferably, be fixed with the drain pipe on the outer wall of cooling tank bottom, the one end and the spiral pipe of drain pipe are linked together, and the bottom of drain pipe installs the control valve, are convenient for derive the inside distillate of spiral pipe.
Preferably, the filter screen is installed to the inside one side of purifying box, and the purifying box internally mounted of filter screen one side has the active carbon adsorption layer, and the active carbon adsorption layer is mutually supported with the filter screen, is convenient for carry out purification treatment to the flue gas.
Preferably, one side that the heating furnace was kept away from to the purifying box is provided with the draught fan, and the input and the purifying box of draught fan communicate mutually, are convenient for take the inside flue gas of heating furnace out.
Preferably, the connecting sleeve is installed to the drain pipe bottom of control valve below, and the bottom mounting of connecting sleeve has flexible pipe to the bottom mounting of flexible pipe has the catheter, and the bottom of catheter extends to the inside of collecting vessel, is convenient for block outside dust impurity, the effectual pollution that reduces the distillate and receive.
Compared with the prior art, the beneficial effects of the utility model are that: the distiller for producing the white spirit not only improves the utilization rate of mist, is convenient for purifying smoke, but also effectively reduces the pollution to distillate;
(1) The cooling tank, the connecting pipe and the spiral pipe are arranged, mist enters the spiral pipe through the connecting pipe, at the moment, cooling liquid in the cooling tank cools the mist in the spiral pipe, and the spiral pipe is of a spiral structure, so that the contact time of the mist and the cooling liquid is prolonged, the gas-liquid conversion is more sufficient, the conversion efficiency is higher, and the utilization rate of the mist is improved;
(2) The smoke in the heating furnace is pumped out by starting the draught fan through the purification box, the filter screen, the activated carbon adsorption layer and the draught fan, the smoke enters the purification box through the smoke exhaust pipe, the filter screen in the purification box filters large granular impurities in the smoke for the first time, and the activated carbon adsorption layer adsorbs harmful substances in the smoke for the second time, so that the smoke is conveniently purified, and the pollution to the atmosphere is reduced;
(3) Through being provided with the adapter sleeve, flexible pipe and catheter, place the collecting vessel under the drain pipe, with the adapter sleeve in the bottom of drain pipe, the flexible pipe of drop-down makes the inside that the catheter of its bottom stretched into the collecting vessel, open the control valve again and make the inside of the inside distillate of spiral pipe through the drain pipe discharge and flow into the collecting vessel under the guide effect of flexible pipe, the setting of flexible pipe can block outside dust impurity, thereby the effectual pollution that the distillate received that has reduced.
Drawings
Fig. 1 is a schematic front view of the present invention;
FIG. 2 is a schematic view of a cross-sectional enlarged structure of the cooling tank of the present invention;
FIG. 3 is a schematic view of the cross-sectional enlarged structure of the purification box of the present invention;
fig. 4 is an enlarged schematic structural diagram of a in fig. 1 according to the present invention.
In the figure: 1. heating furnace; 2. a distillation barrel; 3. a liquid storage tank; 4. a collection barrel; 5. a liquid outlet pipe; 6. a cooling tank; 7. a distillation tube; 8. a smoke exhaust pipe; 9. a purification box; 10. an induced draft fan; 11. a connecting pipe; 12. a spiral tube; 13. a filter screen; 14. an activated carbon adsorption layer; 15. a control valve; 16. connecting sleeves; 17. a telescopic pipe; 18. a catheter.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-4, the present invention provides an embodiment: a distiller for white spirit production comprises a heating furnace 1, a distillation barrel 2, a cooling tank 6, a distillation pipe 7 and a purification box 9, wherein the distillation barrel 2 is installed at the top end of the heating furnace 1, the distillation pipe 7 is fixed at the top end of the distillation barrel 2, the distillation pipe 7 is communicated with the distillation barrel 2, a smoke exhaust pipe 8 is fixed on the outer wall of the top of the heating furnace 1, and the smoke exhaust pipe 8 is communicated with the heating furnace 1;
a spiral pipe 12 is arranged in the cooling tank 6, a connecting pipe 11 is fixed at the top end of the spiral pipe 12, and the top end of the connecting pipe 11 is communicated with the bottom end of the distillation pipe 7, so that the contact time of mist and cooling liquid is prolonged, gas-liquid conversion is more sufficient, and the conversion efficiency is higher;
a purification box 9 is arranged on one side of the heating furnace 1, the purification box 9 is communicated with a smoke exhaust pipe 8, a filter screen 13 is arranged on one side inside the purification box 9, an active carbon adsorption layer 14 is arranged inside the purification box 9 on one side of the filter screen 13, and the active carbon adsorption layer 14 is matched with the filter screen 13, so that the purification treatment of smoke is facilitated;
an induced draft fan 10 is arranged on one side of the purification box 9, which is far away from the heating furnace 1, and the input end of the induced draft fan 10 is communicated with the purification box 9, so that the flue gas in the heating furnace 1 can be conveniently extracted;
a liquid storage tank 3 is arranged on the other side of the heating furnace 1, a cooling tank 6 is fixed at the top end of the liquid storage tank 3, the cooling tank 6 is communicated with the liquid storage tank 3, and a collecting barrel 4 is arranged on one side of the liquid storage tank 3 far away from the heating furnace 1;
a liquid outlet pipe 5 is fixed on the outer wall of the bottom of the cooling tank 6, one end of the liquid outlet pipe 5 is communicated with the spiral pipe 12, and a control valve 15 is installed at the bottom of the liquid outlet pipe 5, so that distillate in the spiral pipe 12 can be conveniently led out;
connecting sleeve 16 is installed to drain pipe 5 bottom below control valve 15, and the bottom of connecting sleeve 16 is fixed with flexible pipe 17 to flexible pipe 17's bottom is fixed with catheter 18, and the bottom of catheter 18 extends to the inside of collecting vessel 4, is convenient for block outside dust impurity, the effectual pollution that reduces the distillate and receive.
The working principle is as follows: when the device is used, firstly, the heating furnace 1 works to heat the distillation barrel 2, fog generated by heating the distillation barrel 2 rises and enters the distillation tube 7, the distillation tube 7 guides the fog into the cooling tank 6, the fog enters the spiral tube 12 through the connecting tube 11, at the moment, the cooling liquid in the cooling tank 6 cools the fog in the spiral tube 12, the fog in the spiral tube 12 is condensed into water drops and flows into the liquid outlet tube 5, because the spiral tube 12 is of a spiral structure, the contact time of the fog and the cooling liquid is prolonged, the gas-liquid conversion is more sufficient, the conversion efficiency is higher, the utilization rate of the fog is improved, then, the collection barrel 4 is placed under the liquid outlet tube 5, and the connecting sleeve 16 is sleeved at the bottom end of the liquid outlet tube 5, draw down flexible pipe 17 and make the catheter 18 of its bottom stretch into the inside of collecting vessel 4, open control valve 15 again and make the inside distillate of spiral pipe 12 discharge through drain pipe 5 and flow into the inside of collecting vessel 4 under flexible pipe 17's guide effect, flexible pipe 17's setting can block outside dust impurity, thereby the effectual pollution that reduces the distillate and receive, finally, start draught fan 10 and make its flue gas with heating furnace 1 inside take out, the flue gas enters into the inside of purifying box 9 through tub 8 that discharges fume, the inside filter screen 13 of purifying box 9 carries out once filtration to the large granule impurity in the flue gas, activated carbon adsorption layer 14 carries out the secondary absorption to the harmful substance in the flue gas, thereby be convenient for carry out purification treatment to the flue gas, the pollution that causes the atmosphere has been reduced, the work of the distiller that is used for white spirit production is accomplished.
It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (6)
1. The utility model provides a distiller for white spirit production, includes heating furnace (1), distillation barrel (2), cooling tank (6), distillation tube (7) and purifying box (9), its characterized in that: distillation barrel (2) are installed on the top of heating furnace (1), and the top of distillation barrel (2) is fixed with distillation tube (7), and distillation tube (7) are linked together with distillation barrel (2) to be fixed with on the outer wall at heating furnace (1) top and discharge fume pipe (8), discharge fume pipe (8) and heating furnace (1) are linked together, one side of heating furnace (1) is provided with purifying box (9), and purifying box (9) and discharge fume pipe (8) are linked together, the opposite side of heating furnace (1) is provided with liquid storage pot (3), and the top of liquid storage pot (3) is fixed with cooling tank (6), and cooling tank (6) are linked together with liquid storage pot (3), one side that heating furnace (1) was kept away from in liquid storage pot (3) is provided with collecting vessel (4).
2. A distiller for white spirit production according to claim 1, characterised in that: the inside of cooling tank (6) is provided with spiral pipe (12), and the top of spiral pipe (12) is fixed with connecting pipe (11), and the top of connecting pipe (11) is linked together with the bottom of distillation tube (7).
3. A distiller for white spirit production according to claim 2, characterised in that: be fixed with drain pipe (5) on the outer wall of cooling tank (6) bottom, the one end and spiral pipe (12) of drain pipe (5) are linked together, and control valve (15) are installed to the bottom of drain pipe (5).
4. A distiller for white spirit production according to claim 1, characterised in that: filter screen (13) are installed to inside one side of purifying box (9), and purifying box (9) internally mounted of filter screen (13) one side has activated carbon adsorption layer (14), and activated carbon adsorption layer (14) and filter screen (13) mutually support.
5. A distiller for white spirit production according to claim 1, characterised in that: one side of the purification box (9) far away from the heating furnace (1) is provided with an induced draft fan (10), and the input end of the induced draft fan (10) is communicated with the purification box (9).
6. A distiller for white spirit production according to claim 3, characterised in that: a connecting sleeve (16) is installed at the bottom end of the liquid outlet pipe (5) below the control valve (15), a telescopic pipe (17) is fixed at the bottom end of the connecting sleeve (16), a liquid guide pipe (18) is fixed at the bottom end of the telescopic pipe (17), and the bottom end of the liquid guide pipe (18) extends into the collecting barrel (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123341930.8U CN217651177U (en) | 2021-12-28 | 2021-12-28 | Distiller for liquor production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202123341930.8U CN217651177U (en) | 2021-12-28 | 2021-12-28 | Distiller for liquor production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN217651177U true CN217651177U (en) | 2022-10-25 |
Family
ID=83659814
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202123341930.8U Expired - Fee Related CN217651177U (en) | 2021-12-28 | 2021-12-28 | Distiller for liquor production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN217651177U (en) |
-
2021
- 2021-12-28 CN CN202123341930.8U patent/CN217651177U/en not_active Expired - Fee Related
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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: 20221025 |