CN112195091A - White spirit distillation plant - Google Patents
White spirit distillation plant Download PDFInfo
- Publication number
- CN112195091A CN112195091A CN202011232295.7A CN202011232295A CN112195091A CN 112195091 A CN112195091 A CN 112195091A CN 202011232295 A CN202011232295 A CN 202011232295A CN 112195091 A CN112195091 A CN 112195091A
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- boiler
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- proof box
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- 238000004821 distillation Methods 0.000 title claims abstract description 21
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 30
- 239000002994 raw material Substances 0.000 claims abstract description 29
- 239000000779 smoke Substances 0.000 claims abstract description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 11
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- 241000208125 Nicotiana Species 0.000 claims abstract description 6
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims abstract description 6
- 235000014101 wine Nutrition 0.000 claims description 46
- 238000001816 cooling Methods 0.000 claims description 32
- 238000002485 combustion reaction Methods 0.000 claims description 23
- 238000007789 sealing Methods 0.000 claims description 18
- 238000003756 stirring Methods 0.000 claims description 16
- 238000005192 partition Methods 0.000 claims description 6
- 241000196324 Embryophyta Species 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000000741 silica gel Substances 0.000 claims description 4
- 229910002027 silica gel Inorganic materials 0.000 claims description 4
- 239000003245 coal Substances 0.000 abstract description 31
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract description 24
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 abstract description 12
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract description 12
- 239000001569 carbon dioxide Substances 0.000 abstract description 12
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 7
- 229910002091 carbon monoxide Inorganic materials 0.000 abstract description 7
- 235000017557 sodium bicarbonate Nutrition 0.000 abstract description 6
- 229910000030 sodium bicarbonate Inorganic materials 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 230000002349 favourable effect Effects 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 10
- 239000010883 coal ash Substances 0.000 description 9
- 239000002699 waste material Substances 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 8
- 238000002156 mixing Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 235000015096 spirit Nutrition 0.000 description 3
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 238000003483 aging Methods 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 239000005457 ice water Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- CVHZOJJKTDOEJC-UHFFFAOYSA-N saccharin Chemical compound C1=CC=C2C(=O)NS(=O)(=O)C2=C1 CVHZOJJKTDOEJC-UHFFFAOYSA-N 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 235000014692 zinc oxide Nutrition 0.000 description 1
- 239000011787 zinc oxide Substances 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H6/00—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
- C12H6/02—Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23Q—IGNITION; EXTINGUISHING-DEVICES
- F23Q13/00—Igniters not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B5/00—Condensers employing a combination of the methods covered by main groups F28B1/00 and F28B3/00; Other condensers
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- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Biochemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Genetics & Genomics (AREA)
- Health & Medical Sciences (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Food Science & Technology (AREA)
- Combustion & Propulsion (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to the technical field of distillation, in particular to a white spirit distillation device, which comprises a boiler, wherein an explosion-proof box is arranged on one side of the boiler, a smoke removing mechanism is arranged in the explosion-proof box, the explosion-proof box is connected with the boiler through a smoke tube, and a raw material box is arranged at the top of the boiler, and has the advantages that: the explosion-proof board divides the inside of explosion-proof box into two sets of spaces, the inside smoke that the inside coal burning of boiler produced passes through the tobacco pipe and gets into the inside of explosion-proof box from the boiler, then control the oxygenerator and start, the point firearm is explosion-proof point firearm, control point firearm ignition, carbon monoxide produces carbon dioxide with the oxygen burning, then carbon dioxide gets into another set of space in the explosion-proof box from the inlet port, sodium hydroxide reacts with carbon dioxide, give birth to sodium bicarbonate and water, be favorable to carrying out the chemical reaction to the smoke that the coal burning produced and handle, prevent that the direct discharge of coal smoke from endangering healthyly, the contaminated air.
Description
Technical Field
The invention relates to the technical field of distillation, in particular to a white spirit distillation device.
Background
Chinese white spirit has compound fragrance with esters as main body, uses yeasts and yeast as saccharification leaven, and uses starchiness (saccharine) as raw material, and is made into various wines by cooking, saccharification, fermentation, distillation, ageing and blending, and in strict sense, the blended wine blended by edible alcohol and edible perfume can not be calculated as white spirit.
The existing white spirit needs to be heated to evaporate fermented grains in the distillation process, coal is needed in the heating process, smoke generated by coal combustion is directly discharged into air, and the existing white spirit is harmful to health and pollutes air; and coal is not fully combusted in the combustion process, so that the heating time of fermented grains is slow, the distillation efficiency is low, the cooling structure of wine vapor is simple, and the cooling efficiency is low.
Disclosure of Invention
The invention aims to solve the defects in the prior art and provides a white spirit distillation device.
In order to achieve the purpose, the invention adopts the following technical scheme:
the design is a white spirit distillation device, which comprises a boiler, one side of boiler is provided with explosion-proof box, explosion-proof box's inside is provided with smoke abatement mechanism, explosion-proof box passes through the tobacco pipe with the boiler and is connected, the top of boiler is provided with the head tank, the top of head tank is provided with the charge door, the inside of boiler is provided with combustion mechanism, one side that explosion-proof box was kept away from to the boiler is provided with the cooler bin, the cooler bin passes through the blast pipe with the head tank and is connected, the inside of cooler bin is provided with cooling mechanism.
Preferably, the smoke abatement mechanism is including the oxygenerator that is located explosion-proof roof portion, the gas outlet of oxygenerator is located explosion-proof roof portion, explosion-proof roof portion is provided with the explosion-proof board, explosion-proof roof portion is provided with the inlet port, explosion-proof roof portion's inner wall is provided with some firearm, one side that explosion-proof roof portion kept away from some firearm is provided with places the board, the intermediate position of placing the board is provided with the recess, the inside of recess is provided with sodium hydroxide, the both sides of placing the board are provided with the through-hole, the bottom of placing the board is provided with the drawer.
Preferably, combustion mechanism includes the boiler, the inside of boiler is provided with the grid plate, the both sides of raw materials tank bottom are provided with the heat-conducting plate, the intermediate position of raw materials tank bottom is provided with the discharge gate, the bottom of discharge gate is provided with the solenoid valve, driving motor is installed to one side of raw materials tank, driving motor's output is connected with the (mixing) shaft, the (mixing) shaft extends to the inside of raw materials tank, the surface of (mixing) shaft is provided with stirring vane.
Preferably, cooling body is including the condenser that is located the cooler bin top, the cold ware gas port of condenser bottom extends to the inside of cooler bin, the lateral wall of cooler bin is provided with the mounting panel, the top of mounting panel is provided with leads cold storehouse, the inside that leads cold storehouse is provided with the baffle, the ice-cube has been placed at the top of baffle, the bottom that leads cold storehouse is provided with the water-collecting box.
Preferably, a wine storage box is arranged on one side of the cooling box and is connected with the cooling box through a circulating pipe, and an outlet is formed in one side of the wine storage box.
Preferably, the top of charge door is provided with the apron, the inside of apron is provided with the sealing washer, the sealing washer is the silica gel sealing washer.
Preferably, the front surface of the explosion-proof box is provided with an explosion-proof door, the joint of the explosion-proof door and the explosion-proof box is provided with an explosion-proof ring, and one side of the explosion-proof door, which is far away from the smoke tube, is provided with an exhaust port.
Preferably, the front surface of boiler is provided with the furnace gate, the furnace gate passes through hinge connection with the boiler, the front surface of cooler bin is provided with sealing door, the furnace gate all is provided with the handle with one side of sealing door.
Preferably, the front end and the tail end of the cold guide bin are both designed to be hollow, and the length of the partition plate is smaller than that of the water collecting box.
Preferably, the electromagnetic valve is a high-temperature resistant electromagnetic valve, and the maximum bearing value of the electromagnetic valve is five hundred degrees centigrade.
The white spirit distillation device provided by the invention has the beneficial effects that:
1. by the arranged oxygen generator, the explosion-proof plate, the air inlet hole, the igniter, the placing plate, the groove, the sodium hydroxide, the through hole and the drawer, the explosion-proof plate divides the interior of the explosion-proof box into two groups of spaces, smoke (main component carbon monoxide) generated by coal combustion in the boiler enters the interior of the explosion-proof box from the boiler through the smoke tube, then the oxygen generator is controlled to start, the igniter is an explosion-proof igniter, the igniter is controlled to ignite, the carbon monoxide and the oxygen are combusted to generate carbon dioxide, then the carbon dioxide enters the other group of spaces in the explosion-proof box from the air inlet hole, the sodium hydroxide reacts with the carbon dioxide to generate sodium bicarbonate and water, then the generated substances fall into the drawer from the through hole, the residual small amount of gas is discharged from the air outlet, then the explosion-proof door is opened, the drawer is taken out, the sodium bicarbonate and the water are poured out, the chemical reaction treatment, polluting the air.
2. Coal is put on the grid plate, the melting point of the grid plate is five hundred ℃, coal ash generated by coal combustion can fall to the bottom of the boiler from the grid plate, the coal is separated from the coal ash, the coal ash is prevented from being accumulated to extinguish coal fire, the coal is fully combusted, the heating efficiency is improved, heat generated by the coal combustion is transferred to a raw material box through the heat conducting plate, the stirring shaft and the stirring blade are driven by the driving motor to rotate, fermented grains in the raw material box are overturned to be uniformly heated, the heating efficiency is further improved, when the fermented grains are completely heated and evaporated into wine steam to enter a cooling box, the electromagnetic valve is controlled to be started, the discharge port is opened at the moment, waste fermented grains enter the boiler, when the fermented grains are used next time, the waste fermented grains are used as combustion raw materials, and waste is utilized, the cost is saved.
3. Through the cooler bin that sets up, the condenser, the mounting panel, lead cold storehouse, a separation plate, the ice-cube, the water catch box, the wine unstrained spirits is heated the evaporation completely and becomes wine steam and passes through the blast pipe and get into the cooler bin, the condenser is tentatively cooled off wine steam, make wine steam liquefaction become wine, the ice-cube absorbs wine steam's heat, make its further liquefaction become wine, be favorable to improving the cooling effect, make its quick liquefaction, then the ice-cube can melt, the frozen water of production can get into in the water catch box.
Drawings
FIG. 1 is a schematic view of a flow structure proposed by the present invention;
FIG. 2 is a schematic view of the internal structure of the explosion-proof box according to the present invention;
FIG. 3 is a schematic view of the internal structure of the boiler and the raw material tank according to the present invention;
fig. 4 is a schematic structural diagram of the position a according to the present invention.
FIG. 5 is a schematic view of a grid plate structure according to the present invention
FIG. 6 is a schematic view of the internal structure of the cooling box according to the present invention
FIG. 7 is a schematic view of the internal structure of the cold guide bin according to the present invention
In the figure: 1. a boiler; 101. a grid plate; 102. a heat conducting plate; 103. a discharge port; 104. an electromagnetic valve; 105. a drive motor; 106. a stirring shaft; 107. a stirring blade; 2. an explosion-proof box; 3. a smoke pipe; 4. a raw material tank; 5. a feed inlet; 6. a cooling tank; 601. a condenser; 602. mounting a plate; 603. a cold guide bin; 604. a partition plate; 605. ice cubes; 606. a water collection box; 7. an exhaust pipe; 8. an oxygen generator; 801. an explosion-proof plate; 802. an air inlet; 803. an igniter; 804. placing the plate; 805. a groove; 806. sodium hydroxide; 807. a through hole; 808. a drawer; 9. a wine storage box; 10. a flow-through tube; 11. an outlet; 12. an explosion vent; 13. an exhaust port; 14. a furnace door; 15. and (4) sealing the door.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments.
Referring to fig. 1-7, a white spirit distillation plant, including boiler 1, one side of boiler 1 is provided with explosion-proof box 2, the inside of explosion-proof box 2 is provided with smoke abatement mechanism, explosion-proof box 2 is connected through tobacco pipe 3 with boiler 1, the top of boiler 1 is provided with feed tank 4, the top of feed tank 4 is provided with charge door 5, the inside of boiler 1 is provided with combustion mechanism, one side that boiler 1 kept away from explosion-proof box 2 is provided with cooler bin 6, cooler bin 6 is connected through blast pipe 7 with feed tank 4, the inside of cooler bin 6 is provided with cooling mechanism.
Through setting up tobacco pipe 3, in the coal smoke entering explosion-proof box 2 in the boiler 1 of being convenient for, the charge door 5 of setting is convenient for add the wine unstrained spirits to the raw materials box 4 in, through setting up blast pipe 7, is convenient for wine steam from the raw materials box entering cooling tank 6 in.
Wherein, smoke abatement mechanism is including being located the oxygenerator 8 at explosion-proof box 2 top, the gas outlet of oxygenerator 8 is located explosion-proof box 2's inside, explosion-proof box 2's inside is provided with explosion-proof plate 801, explosion-proof plate 801's top is provided with inlet port 802, explosion-proof box 2's inner wall is provided with some firearm 803, explosion-proof box 2 keeps away from one side of some firearm 803 and is provided with and places board 804, the intermediate position of placing board 804 is provided with recess 805, the inside of recess 805 is provided with sodium hydroxide 806, the both sides of placing board 804 are provided with the through-hole 807, the bottom of placing board 804 is provided with drawer.
By the arrangement of the oxygen generator 8, the explosion-proof plate 801, the air inlet hole 802, the igniter 803, the placing plate 804, the groove 805, the sodium hydroxide 806, the through hole 807 and the drawer 808, the explosion-proof plate 801 divides the interior of the explosion-proof box 2 into two groups of spaces, smoke (carbon monoxide as a main component) generated by coal combustion in the boiler 1 enters the interior of the explosion-proof box 2 from the boiler 1 through the smoke pipe 3, then the oxygen generator 8 is controlled to start, the igniter 803 is an explosion-proof igniter, the igniter 803 is controlled to ignite, the carbon monoxide and the oxygen are combusted to generate carbon dioxide, then the carbon dioxide enters the other group of spaces in the explosion-proof box 2 from the air inlet hole 802, the sodium hydroxide 806 reacts with the carbon dioxide to generate sodium bicarbonate and water, then the generated substances fall into the drawer 808 from the through hole 807, the residual small amount of gas is discharged from the air outlet 13, then the explosion-proof door 12, the smoke generated by coal combustion is favorably subjected to chemical reaction treatment, and the direct discharge of the soot, which is harmful to health, and pollutes air is prevented.
Wherein, combustion mechanism includes boiler 1, and boiler 1's inside is provided with grid plate 101, and the both sides of raw materials case 4 bottom are provided with heat-conducting plate 102, and the intermediate position of raw materials case 4 bottom is provided with discharge gate 103, and the bottom of discharge gate 103 is provided with solenoid valve 104, and driving motor 105 is installed to one side of raw materials case 4, and driving motor 105's output is connected with (mixing) shaft 106, and (mixing) shaft 106 extends to the inside of raw materials case 4, and the surface of (mixing) shaft 106 is provided with stirring vane 107.
Coal is put on the grid plate 101 through the arranged boiler 1, the grid plate 101, the heat conduction plate 102, the discharge hole 103, the electromagnetic valve 104, the driving motor 105, the stirring shaft 106 and the stirring blade 107, the melting point of the grid plate 101 is five hundred ℃, the coal ash generated by coal combustion can fall to the bottom of the boiler 1 from the grid plate 101, the coal is separated from the coal ash, the coal ash is prevented from being accumulated to extinguish the coal fire, the coal is fully combusted, the heating efficiency is improved, the heat generated by coal combustion is transferred to the raw material box 4 through the heat conduction plate 102, the driving motor 105 drives the stirring shaft 106 and the stirring blade 107 to rotate, the fermented grains in the raw material box 4 are overturned to be uniformly heated, the heating efficiency is further improved, when the fermented grains are completely heated and evaporated into wine steam to enter the cooling box 6, the electromagnetic valve 104 is controlled to be started, the discharge hole 103 is opened at the moment, the waste fermented grains enter the boiler 1, and, the waste fermented grains are used as combustion raw materials, so that the waste is utilized, and the cost is saved.
Wherein, cooling body is including being located the condenser 601 at cooler bin 6 top, and the cold ware gas port of condenser 601 bottom extends to the inside of cooler bin 6, and the lateral wall of cooler bin 6 is provided with mounting panel 602, and the top of mounting panel 602 is provided with leads cold storehouse 603, and the inside of leading cold storehouse 603 is provided with baffle 604, and ice-cube 605 has been placed at the top of baffle 604, and the bottom of leading cold storehouse 603 is provided with water-collecting box 606.
Through the cooler bin 6 that sets up, condenser 601, mounting panel 602, lead cold storehouse 603, baffle 604, ice-cube 605, water catch box 606, the unstrained spirits are heated completely and evaporate into wine steam and pass through blast pipe 7 entering cooler bin 6, condenser 601 cools off wine steam tentatively, make wine steam liquefaction become wine, ice-cube 605 absorbs the heat of wine steam, make its further liquefaction become wine, be favorable to improving the cooling effect, make its fast liquefaction, then ice-cube 605 can melt, the frozen water of production can get into in the water catch box 606.
Wherein, one side of the cooling box 6 is provided with a wine storage box 9, the wine storage box 9 is connected with the cooling box 6 through a circulating pipe 10, and one side of the wine storage box 9 is provided with an outlet 11.
Through setting up wine storage box 9 and runner pipe 10, the wine steam cooling liquefaction in the cooler bin 6 of being convenient for gets into through runner pipe 10 and stores up in wine storage box 9, sets up export 11, is convenient for make the wine that stores up in the wine storage box 9 flow out.
Wherein, the top of charge door 5 is provided with the apron, and the inside of apron is provided with the sealing washer, and the sealing washer is the silica gel sealing washer.
Through the apron that sets up, be convenient for prevent that impurity from getting into, and can prevent that steam from spilling, the silica gel sealing washer of setting can improve sealed effect, further prevents that wine steam from spilling.
Wherein, the front surface of explosion-proof box 2 is provided with explosion-proof door 12, and the junction of explosion-proof door 12 and explosion-proof box 2 is provided with the explosion-proof circle, and explosion-proof door 12 is provided with gas vent 13 away from one side of tobacco pipe 3.
Through setting up explosion vent 12, be convenient for open explosion-proof box 2, explosion-proof circle can improve explosion-proof effect, and other a small amount of gas discharges are convenient for to gas vent 13.
Wherein, the front surface of the boiler 1 is provided with a furnace door 14, the furnace door 14 is connected with the boiler 1 through a hinge, the front surface of the cooling box 6 is provided with a sealing door 15, and handles are arranged on one sides of the furnace door 14 and the sealing door 15.
The furnace door 14 is convenient to open through the arranged furnace door 14, coal is added into the boiler 1, the cooling box 6 is convenient to open through the arranged sealing door 15, and the sealing door 15 is convenient to pull through the handle.
The front end and the tail end of the cold guide bin 603 are both hollow, and the length of the partition plate 604 is smaller than that of the water collecting box 606.
The front end and the tail end of the cold guide bin 603 are hollow, so that cold air brought by ice blocks 605 can be conveniently transferred, and the cooling effect is improved.
The solenoid valve 104 is a high temperature resistant solenoid valve, and the maximum bearing value thereof is five hundred degrees celsius.
By setting the solenoid valve 104 as a high temperature resistant solenoid valve, the solenoid valve 104 can be made intact under the continuous combustion of a carbon fire.
The working principle is as follows: when the device is used, fermented grains are put into the raw material tank 4 from the feeding port 5, the furnace door 14 is opened, coal is put on the grid plate 101, the melting point of the grid plate 101 is five hundred ℃, coal ash generated by coal combustion falls to the bottom of the boiler 1 from the grid plate 101, the coal is separated from the coal ash, coal ash accumulation is prevented, coal fire is extinguished, coal is fully combusted, heating efficiency is improved, heat generated by coal combustion is transferred to the raw material tank 4 through the heat conduction plate 102, the driving motor 105 drives the stirring shaft 106 and the stirring blades 107 to rotate, the fermented grains in the raw material tank 4 are overturned to be uniformly heated, heating efficiency is further improved, when the fermented grains are completely heated and evaporated into fermented grains steam to enter the cooling tank 6, the electromagnetic valve 104 is controlled to be started, the discharge port 103 is opened at the moment, waste fermented grains enter the boiler 1, when the waste fermented grains are used next time, the waste fermented grains are used as combustion raw materials and are utilized, the cost is saved, in the process of coal combustion, smoke (main component carbon monoxide) generated by coal combustion in a boiler 1 enters the interior of an explosion-proof box 2 from the boiler 1 through a smoke pipe 3, then an oxygenerator 8 is controlled to start, an igniter 803 is an explosion-proof igniter, the igniter 803 is controlled to ignite, the carbon monoxide and oxygen are combusted to generate carbon dioxide, then the carbon dioxide enters another group of space in the explosion-proof box 2 from an air inlet hole 802, sodium hydroxide 806 reacts with the carbon dioxide to generate sodium bicarbonate and water, then a resultant falls into a drawer 808 from a through hole 807, a small amount of residual gas is discharged from an air outlet 13, then an explosion-proof door 12 is opened, a drawer 808 is taken out, the sodium bicarbonate and the water are poured out, after fermented grains in a raw material box 4 are completely heated, the fermented grains are evaporated into wine steam, the wine steam enters a cooling box 6 through an air outlet pipe 7, a condenser 601 preliminarily cools the wine steam to ensure that the, the ice cake 605 absorbs the heat of the wine vapor to further liquefy the wine vapor into wine, the cooling effect is improved, the wine vapor is quickly liquefied, then the ice cake 605 is melted, the generated ice water enters the water collecting box 606, then the wine liquefied by the wine vapor enters the wine storage box 9 through the circulating pipe 10, and finally the wine is discharged through the outlet 11, so that the whole distillation process is completed.
The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and the technical solutions and the inventive concepts thereof according to the present invention should be equivalent or changed within the scope of the present invention.
Claims (10)
1. The utility model provides a white spirit distillation plant, includes boiler (1), its characterized in that: one side of boiler (1) is provided with explosion-proof case (2), the inside of explosion-proof case (2) is provided with smoke abatement mechanism, explosion-proof case (2) are connected through tobacco pipe (3) with boiler (1), the top of boiler (1) is provided with feed box (4), the top of feed box (4) is provided with charge door (5), the inside of boiler (1) is provided with combustion mechanism, one side that explosion-proof case (2) were kept away from in boiler (1) is provided with cooler bin (6), cooler bin (6) are connected through blast pipe (7) with feed box (4), the inside of cooler bin (6) is provided with cooling body.
2. A white spirit distillation apparatus according to claim 1, characterized in that the smoke abatement mechanism comprises an oxygen generator (8) located at the top of an explosion-proof box (2), the air outlet of the oxygen generator (8) is located inside the explosion-proof box (2), an explosion-proof plate (801) is arranged inside the explosion-proof box (2), an air inlet hole (802) is arranged at the top of the explosion-proof plate (801), an igniter (803) is arranged on the inner wall of the explosion-proof box (2), a placing plate (804) is arranged on one side of the explosion-proof box (2) far away from the igniter (803), a groove (805) is arranged at the middle position of the placing plate (804), sodium hydroxide (806) is arranged inside the groove (805), through holes (807) are arranged on two sides of the placing plate (804), and a drawer (808) is arranged at the bottom of the placing plate (804).
3. A white spirit distillation plant according to claim 1, characterized in that the combustion mechanism comprises a boiler (1), a grid plate (101) is arranged inside the boiler (1), heat conducting plates (102) are arranged on two sides of the bottom of the raw material tank (4), a discharge hole (103) is arranged in the middle of the bottom of the raw material tank (4), an electromagnetic valve (104) is arranged at the bottom of the discharge hole (103), a driving motor (105) is installed on one side of the raw material tank (4), a stirring shaft (106) is connected to the output end of the driving motor (105), the stirring shaft (106) extends to the inside of the raw material tank (4), and stirring blades (107) are arranged on the outer surface of the stirring shaft (106).
4. A liquor distilling apparatus according to claim 1, characterized in that the cooling mechanism comprises a condenser (601) located at the top of the cooling tank (6), a cooler air port at the bottom of the condenser (601) extends to the inside of the cooling tank (6), a mounting plate (602) is arranged on the side wall of the cooling tank (6), a cold guiding bin (603) is arranged at the top of the mounting plate (602), a partition plate (604) is arranged inside the cold guiding bin (603), ice blocks (605) are placed at the top of the partition plate (604), and a water collecting box (606) is arranged at the bottom of the cold guiding bin (603).
5. A white spirit distillation unit according to claim 1, characterized in that a wine storage tank (9) is arranged on one side of the cooling tank (6), the wine storage tank (9) is connected with the cooling tank (6) through a flow pipe (10), and an outlet (11) is arranged on one side of the wine storage tank (9).
6. A white spirit distillation device according to claim 1, characterized in that a cover plate is arranged on the top of the feed inlet (5), and a sealing ring is arranged inside the cover plate and is a silica gel sealing ring.
7. A white spirit distillation apparatus according to claim 1, characterized in that the front surface of the explosion-proof box (2) is provided with an explosion-proof door (12), the joint of the explosion-proof door (12) and the explosion-proof box (2) is provided with an explosion-proof ring, and one side of the explosion-proof door (12) far away from the smoke tube (3) is provided with an exhaust port (13).
8. A white spirit distilling apparatus according to claim 1, characterized in that the front surface of the boiler (1) is provided with an oven door (14), the oven door (14) is connected with the boiler (1) through a hinge, the front surface of the cooling box (6) is provided with a sealing door (15), and one side of the oven door (14) and one side of the sealing door (15) are provided with handles.
9. A liquor distilling apparatus according to claim 4, characterised in that the front end and the tail end of the cold guiding bin (603) are both hollow, and the length of the partition plate (604) is smaller than that of the water collecting box (606).
10. A spirit distillation apparatus according to claim 3, wherein the solenoid valve (104) is a high temperature resistant solenoid valve with a maximum tolerance of five hundred degrees Celsius.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011232295.7A CN112195091A (en) | 2020-11-06 | 2020-11-06 | White spirit distillation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202011232295.7A CN112195091A (en) | 2020-11-06 | 2020-11-06 | White spirit distillation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112195091A true CN112195091A (en) | 2021-01-08 |
Family
ID=74034187
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202011232295.7A Pending CN112195091A (en) | 2020-11-06 | 2020-11-06 | White spirit distillation plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112195091A (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203582843U (en) * | 2013-09-10 | 2014-05-07 | 河北农业大学 | Energy-saving and environment-friendly wine steaming equipment |
| CN105588101A (en) * | 2016-03-13 | 2016-05-18 | 林丽芳 | Energy-saving and environment-friendly boiler |
| CN205307836U (en) * | 2016-01-30 | 2016-06-15 | 黑龙江省华裕检测技术有限公司 | Integrated universal distiller |
| CN208346126U (en) * | 2018-05-24 | 2019-01-08 | 河南蔡洪坊酒业有限公司 | Fermented grain distilling apparatus |
| CN209260048U (en) * | 2018-12-01 | 2019-08-16 | 刘晶晶 | A kind of wine brewing distilling apparatus |
-
2020
- 2020-11-06 CN CN202011232295.7A patent/CN112195091A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN203582843U (en) * | 2013-09-10 | 2014-05-07 | 河北农业大学 | Energy-saving and environment-friendly wine steaming equipment |
| CN205307836U (en) * | 2016-01-30 | 2016-06-15 | 黑龙江省华裕检测技术有限公司 | Integrated universal distiller |
| CN105588101A (en) * | 2016-03-13 | 2016-05-18 | 林丽芳 | Energy-saving and environment-friendly boiler |
| CN208346126U (en) * | 2018-05-24 | 2019-01-08 | 河南蔡洪坊酒业有限公司 | Fermented grain distilling apparatus |
| CN209260048U (en) * | 2018-12-01 | 2019-08-16 | 刘晶晶 | A kind of wine brewing distilling apparatus |
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Application publication date: 20210108 |