CN106834055A - Liquor distilling system with function of recovering waste heat - Google Patents

Liquor distilling system with function of recovering waste heat Download PDF

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Publication number
CN106834055A
CN106834055A CN201611242383.9A CN201611242383A CN106834055A CN 106834055 A CN106834055 A CN 106834055A CN 201611242383 A CN201611242383 A CN 201611242383A CN 106834055 A CN106834055 A CN 106834055A
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CN
China
Prior art keywords
heat exchanger
heat
cavity
exhaust outlet
pipe
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Pending
Application number
CN201611242383.9A
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Chinese (zh)
Inventor
蓸均彬
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jia Li Wine Co Ltd Of Chongqing City
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Jia Li Wine Co Ltd Of Chongqing City
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Application filed by Jia Li Wine Co Ltd Of Chongqing City filed Critical Jia Li Wine Co Ltd Of Chongqing City
Priority to CN201611242383.9A priority Critical patent/CN106834055A/en
Publication of CN106834055A publication Critical patent/CN106834055A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12HPASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
    • C12H6/00Methods for increasing the alcohol content of fermented solutions or alcoholic beverages
    • C12H6/02Methods for increasing the alcohol content of fermented solutions or alcoholic beverages by distillation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Biochemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Food Science & Technology (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

The invention discloses a kind of liquor distilling system with function of recovering waste heat, including Liquor distillation pot, First Heat Exchanger, the second heat exchanger and purifying column;Exhaust outlet I is provided with the top of the Liquor distillation pot;The First Heat Exchanger includes shell and heat exchanger tube, and heat exchanging chamber is provided with inside the shell, and the heat exchanger tube is serpentine-like and is respectively arranged at two ends with the first water inlet and the first delivery port;Second heat exchanger includes the not connected epicoele and cavity of resorption that dividing plate and dividing plate are divided into, and the epicoele and cavity of resorption be arranged in parallel;The intracavity bottom of the purifying column is provided with air inlet V, and the inner chamber of purifying column is provided with the shower for spraying weakly alkaline solution, and the bottom of purifying column inner chamber is provided with the solution cavity for containing weakly alkaline solution;The present invention can deal carefully with to white liquor distilling waste gas, saving heat energy loss.

Description

Liquor distilling system with function of recovering waste heat
Technical field
The present invention relates to technical field of brewage, more particularly to a kind of liquor distilling system with function of recovering waste heat.
Background technology
The main component of white wine is ethanol (alcohol) and water (accounting for the 98%~99% of total amount);As a kind of wine of high concentration Smart beverage, the alcohol content of white wine is higher, generally 30~65 degree.Also contain the micro- of the huge numbers such as acid, ester, alcohol, aldehyde in addition Weight organic compounds (account for 1% one the 2% of total amount), they as white wine in fragrant, non-irrigated taste material, decide white wine style and Quality.The chemical energy 70% of ethanol can be immediately used by the body, and 1 gram of ethanol heat supply can be 5 kilocalories.The materials such as acid, ester, alcohol, aldehyde are not How many nutrition, is used only to form the distinctive fragrance of white wine.
In existing process, inflator was removed after still-process, the large quantity of exhaust gas allowed in Liquor distillation pot is expelled directly out, waste gas It is interior to also have organic acid and inorganic acid, corrosion easily is caused to steaming wine workshop, while also occurring in that the air quality steamed in wine workshop Difference, the problems such as workman's respiratory tract is stimulated.Substantial amounts of waste gas has taken away substantial amounts of heat energy, is a kind of invisible wave for enterprise Take, be a kind of invisible destruction for environmental protection.
The content of the invention
In view of this, it is an object of the invention to provide a kind of liquor distilling system with function of recovering waste heat, can White liquor distilling waste gas is dealt carefully with, saving heat energy loss.
Liquor distilling system with function of recovering waste heat of the invention, including Liquor distillation pot, First Heat Exchanger, the second heat exchange Device and purifying column;Exhaust outlet I is provided with the top of the Liquor distillation pot;
The First Heat Exchanger includes shell and heat exchanger tube, and heat exchanging chamber is provided with inside the shell, and the heat exchanger tube is in snake Shape and it is respectively arranged at two ends with the first water inlet and the first delivery port;The heat exchanger tube is applied in heat exchanging chamber and through the shell Top end face, the two ends of heat exchanger tube is communicated with the outside of shell respectively;The shell be provided with positioned at left end air inlet II and Positioned at the exhaust outlet II of right-hand member, the air inlet II is connected with exhaust outlet I by breather pipe I;
Second heat exchanger includes the not connected epicoele and cavity of resorption that is divided into of dividing plate and dividing plate, the epicoele and Cavity of resorption be arranged in parallel;Heat pipe is installed with the dividing plate, the heat pipe is the internal graphite sealed filled with working medium and two ends Pipe, its two ends are in epicoele and cavity of resorption respectively, and fin is provided with the heat pipe outer wall;The left and right two ends difference of the epicoele The second water inlet and the second delivery port are provided with, the left and right of the cavity of resorption is respectively arranged at two ends with air inlet III and exhaust outlet III, described Air inlet III is connected with exhaust outlet II;
The purifying column is provided with air inlet V, and the inner chamber of purifying column is provided with the shower for spraying weakly alkaline solution, The bottom of purifying column inner chamber is provided with the solution cavity for containing weakly alkaline solution;The air inlet V is with exhaust outlet III by ventilation Pipe II is connected;The solution cavity is connected with shower by a circulation pipe, is provided with circulation pipe for by solution cavity Weakly alkaline solution is pumped to the water pump of shower;
The system also includes automatic control system;The automatic control system includes controller, is located at first water inlet Valve is controlled for control water-carrying capacity first, be located at second water inlet for controlling the second control valve of water-carrying capacity at mouthful Be located at the exhaust outlet III be used for real-time detection EGT temperature sensor;The signal output of the temperature sensor End is connected with the signal input part of controller, the signal input part of the first control valve, the signal input part of the second control valve The first signal output part respectively with controller, secondary signal output end are connected.
As a further improvement, the shower is provided with shower nozzle, and the nozzle of the shower nozzle sets up.
As a further improvement, the breather pipe I is provided with the air exhauster for pumping high-temp waste gas.
As a further improvement, the breather pipe I is provided with the high-temperature valve for control pipeline switch.
As a further improvement, the controller is single-chip microcomputer.
Therefore, apply the technical scheme of the present invention, have the advantages that:
Liquor distilling system with function of recovering waste heat of the invention, can effectively by the high-temp waste gas in Liquor distillation pot Discharged after purification, prevent the air pollution in workshop, be conducive to the health of workman;Pass through two-stage heat exchanger pair in purification process Heat energy is recycled, and so as to be dealt carefully with to white liquor distilling waste gas, saving heat energy loss had not only been saved cost but also reached Environmental requirement is arrived.
Brief description of the drawings
The invention will be further described with reference to the accompanying drawings and examples:
Fig. 1 is structural representation of the invention;
Fig. 2 is the theory diagram of automatic control system of the invention.
Specific embodiment
As shown in the figure:The liquor distilling system with function of recovering waste heat of the present embodiment, including Liquor distillation pot 1, first change Hot device, the second heat exchanger and purifying column 4;The top of the Liquor distillation pot 1 is provided with exhaust outlet I 11.
The First Heat Exchanger includes shell 21 and heat exchanger tube 22, and heat exchanging chamber 23 is provided with inside the shell 21, described to change Heat pipe 22 is serpentine-like and is respectively arranged at two ends with the first water inlet 22a and the first delivery port 22b;The heat exchanger tube 22 is applied in heat exchange In chamber 23 and through the top end face of the shell 21, communicate outside of the two ends of heat exchanger tube 22 respectively with shell 21;The pipe Shell 21 is provided with the 21a of air inlet II positioned at left end and exhaust outlet II 21b, the 21a of the air inlet II positioned at right-hand member and exhaust outlet I 11 are connected by breather pipe I 5;The snakelike heat exchange area of heat exchanger tube 22 is larger, and heat transfer effect is preferable;It is to improve heat transfer point Number, can be set some spoilers in heat exchanging chamber 23, strengthen tail gas turbulent extent, force tail gas to be repeatedly in contact with heat exchanger tube 22; Breather pipe I 5 can be attached by the ring flange at two ends;For ease of control, the breather pipe I 5 is provided with for control pipeline The high-temperature valve 6 of switch;It is that exhaust treatment efficiency is improved according to situation, is additionally provided with for pumping high-temp waste gas on the breather pipe I 5 Air exhauster 8;
Second heat exchanger includes the not connected epicoele 32 and cavity of resorption 33 that dividing plate 31 and dividing plate 31 are divided into, institute State epicoele 32 and cavity of resorption 33 be arranged in parallel;Heat pipe 34 is installed with the dividing plate 31, the heat pipe 34 is inside filled with work Matter and the graphite-pipe of two ends sealing, its two ends are in epicoele 32 and cavity of resorption 33 respectively, and wing is provided with the outer wall of the heat pipe 34 Piece 35;The left and right of the epicoele 32 is respectively arranged at two ends with the second water inlet 32a and the second delivery port 32b, a left side for the cavity of resorption 33 The right side is respectively arranged at two ends with the 33a of air inlet III and exhaust outlet III 33b, the 33a of the air inlet III are connected with the 21b of exhaust outlet II;Heat Pipe 34 relies on phase-change heat transfer, thus heat pipe 34 internal thermal resistance very little, so the larger coefficient of overall heat transmission can be obtained with the less temperature difference; Graphite has good thermal conductivity, and with good chemical stability, plasticity and thermal shock resistance, can be acidproof, alkaline-resisting and resistance to The corrosion of organic solvent;Fin 35 can increase the area of heat exchange, lift the effect of heat exchange.
The purifying column 4 is provided with air inlet V 41, and the inner chamber of purifying column 4 is provided with the spray for spraying weakly alkaline solution Pipe 42, the bottom of purifying column inner chamber is provided with the solution cavity 43 for containing weakly alkaline solution;The air inlet V 41 and exhaust outlet III 33b is connected by breather pipe II 7;The solution cavity 43 is connected with shower 42 by a circulation pipe 44, circulation pipe 44 In be provided with water pump 45 for the weakly alkaline solution in solution cavity 43 to be pumped to shower 42;The structure can realize purifying column Weakly alkaline solution is recycled in 4, while improving gas cleaning efficiency;Additionally, the shower 42 is provided with shower nozzle 46, institute The nozzle for stating shower nozzle 46 sets up;When using shower nozzle 46 upwards sprinkling weakly alkaline solution, upwards motion weakly alkaline solution with The smoke contacts of rising and realize purification, while the weakly alkaline solution moved downward by gravity also with rise smoke contacts and Improve degree of purification.
The system also includes automatic control system;The automatic control system includes controller 81, is located at described first and enters Valve 82 is controlled for control water-carrying capacity first, be located at the second water inlet 32a for controlling water-carrying capacity at the 22a of the mouth of a river Second controls valve 83 and is located at the temperature sensor 84 at the 33b of the exhaust outlet III for real-time detection EGT;The temperature The signal output part for spending sensor 84 is connected with the signal input part of controller 81, the signal input of the first control valve 82 End, signal input part first signal output part respectively with controller 81 of the second control valve 83, secondary signal output end are connected; The first control control valve 83 of valve 82, second is automatically controlled valve arrangement;Waste gas at the 33b of 84 real-time detection exhaust outlet of temperature sensor III Temperature, when temperature exceed 81 preset value of controller when, controller 81 to first control valve 82 and second control valve 83 send increasing The signal of big flow, to reduce EGT rapidly;When EGT is less than 81 preset value of controller, controller 81 is to first The control control valve 83 of valve 82 and second sends the signal for reducing flow, to properly increase EGT, waste gas is suitable in purification Tower 4 is reacted, and keeps larger purification efficiency.
Finally illustrate, above-described embodiment is the present invention preferably implementation method, but embodiments of the present invention are not Be restricted to the described embodiments, it is other it is any without departing from the change made under Spirit Essence of the invention and principle, modify, replace Generation, combination, simplification, should be equivalent substitute mode, be included within protection scope of the present invention.

Claims (5)

1. a kind of liquor distilling system with function of recovering waste heat, it is characterised in that:Including Liquor distillation pot, First Heat Exchanger, Two heat exchangers and purifying column;Exhaust outlet I is provided with the top of the Liquor distillation pot;
The First Heat Exchanger includes shell and heat exchanger tube, is provided with heat exchanging chamber inside the shell, the heat exchanger tube it is serpentine-like and It is respectively arranged at two ends with the first water inlet and the first delivery port;The heat exchanger tube is applied in heat exchanging chamber and through the top of the shell End face, makes the two ends of heat exchanger tube be communicated with the outside of shell respectively;The shell be provided with positioned at left end air inlet II and be located at The exhaust outlet II of right-hand member, the air inlet II is connected with exhaust outlet I by breather pipe I;
Second heat exchanger includes the not connected epicoele and cavity of resorption that dividing plate and dividing plate are divided into, the epicoele and cavity of resorption It is arranged in parallel;Heat pipe is installed with the dividing plate, the heat pipe is the internal graphite-pipe sealed filled with working medium and two ends, its Two ends are in epicoele and cavity of resorption respectively, and fin is provided with the heat pipe outer wall;The left and right of the epicoele is respectively arranged at two ends with Second water inlet and the second delivery port, the left and right of the cavity of resorption are respectively arranged at two ends with air inlet III and exhaust outlet III, the air inlet Mouth III is connected with exhaust outlet II;
The purifying column is provided with air inlet V, and the inner chamber of purifying column is provided with the shower for spraying weakly alkaline solution, purification The bottom of tower inner chamber is provided with the solution cavity for containing weakly alkaline solution;The air inlet V passes through breather pipe II with exhaust outlet III It is connected;The solution cavity is connected with shower by a circulation pipe, is provided with circulation pipe for by the weak base in solution cavity Property solution is pumped to the water pump of shower;
The system also includes automatic control system;The automatic control system includes controller, is located at first water inlet For controlling water-carrying capacity first controls valve, is located at second water inlet for controlling the second control valve of water-carrying capacity and setting It is used for the temperature sensor of real-time detection EGT at the exhaust outlet III;The signal output part of the temperature sensor with The signal input part of controller is connected, the signal input part of the first control valve, the signal input part difference of the second control valve The first signal output part, secondary signal output end with controller are connected.
2. the liquor distilling system with function of recovering waste heat according to claim 1, it is characterised in that:The shower Shower nozzle is provided with, the nozzle of the shower nozzle sets up.
3. the liquor distilling system with function of recovering waste heat according to claim 2, it is characterised in that:The breather pipe I is provided with the air exhauster for pumping high-temp waste gas.
4. the liquor distilling system with function of recovering waste heat according to claim 3, it is characterised in that:The breather pipe I is provided with the high-temperature valve for control pipeline switch.
5. the liquor distilling system with function of recovering waste heat according to claim 4, it is characterised in that:The controller It is single-chip microcomputer.
CN201611242383.9A 2016-12-29 2016-12-29 Liquor distilling system with function of recovering waste heat Pending CN106834055A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611242383.9A CN106834055A (en) 2016-12-29 2016-12-29 Liquor distilling system with function of recovering waste heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611242383.9A CN106834055A (en) 2016-12-29 2016-12-29 Liquor distilling system with function of recovering waste heat

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CN106834055A true CN106834055A (en) 2017-06-13

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CN201611242383.9A Pending CN106834055A (en) 2016-12-29 2016-12-29 Liquor distilling system with function of recovering waste heat

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114832573A (en) * 2022-05-23 2022-08-02 江苏益元泰生物技术有限公司 Intelligent control VOCs waste gas integrated treatment method for white spirit production workshop

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202371935U (en) * 2011-11-28 2012-08-08 成都槟果科技有限公司 Heat pipe exchanger
CN204097444U (en) * 2014-08-11 2015-01-14 河南老窖酒业有限公司 Waste heat utilization system in a kind of white liquor distilling technique
CN204097445U (en) * 2014-08-11 2015-01-14 河南老窖酒业有限公司 A kind of environment-friendly type white liquor distilling blowdown system

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN202371935U (en) * 2011-11-28 2012-08-08 成都槟果科技有限公司 Heat pipe exchanger
CN204097444U (en) * 2014-08-11 2015-01-14 河南老窖酒业有限公司 Waste heat utilization system in a kind of white liquor distilling technique
CN204097445U (en) * 2014-08-11 2015-01-14 河南老窖酒业有限公司 A kind of environment-friendly type white liquor distilling blowdown system

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
张磊等: "《电厂锅炉湿法脱硫设备检修技术》", 31 July 2015, 中国电力出版社 *
李玉云: "《建筑设备自动化》", 31 January 2016, 机械工业出版社 *
西安交通大学 郁永章: "《热泵原理与应用》", 30 April 1993, 机械工业出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114832573A (en) * 2022-05-23 2022-08-02 江苏益元泰生物技术有限公司 Intelligent control VOCs waste gas integrated treatment method for white spirit production workshop

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