CN204185461U - Spiral white liquor distilling unit - Google Patents

Spiral white liquor distilling unit Download PDF

Info

Publication number
CN204185461U
CN204185461U CN201420522733.7U CN201420522733U CN204185461U CN 204185461 U CN204185461 U CN 204185461U CN 201420522733 U CN201420522733 U CN 201420522733U CN 204185461 U CN204185461 U CN 204185461U
Authority
CN
China
Prior art keywords
cooling medium
spiral
pipe
buffer chamber
liquid collecting
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Fee Related
Application number
CN201420522733.7U
Other languages
Chinese (zh)
Inventor
王艺成
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.)
CHONGQING ANTAO LIQUOR Co Ltd
Original Assignee
CHONGQING ANTAO LIQUOR Co Ltd
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.)
Filing date
Publication date
Application filed by CHONGQING ANTAO LIQUOR Co Ltd filed Critical CHONGQING ANTAO LIQUOR Co Ltd
Priority to CN201420522733.7U priority Critical patent/CN204185461U/en
Application granted granted Critical
Publication of CN204185461U publication Critical patent/CN204185461U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model discloses a kind of spiral white liquor distilling unit, comprise rice steamer bucket and condenser, steam-pipe is adopted to be connected between rice steamer bucket and condenser, condenser comprises the steam buffer chamber being positioned at upper end and the phlegma liquid collecting cavity being positioned at lower end, condensing unit is provided with between steam buffer chamber and phlegma liquid collecting cavity, steam-pipe is connected with steam buffer chamber, and the bottom of phlegma liquid collecting cavity is provided with phlegma drain pipe; Condensing unit comprises spiral prolong, spiral prolong comprises the two condensation straight tubes be connected with phlegma liquid collecting cavity with steam buffer chamber respectively, spiral cold-finger is connected with between two condensation straight tubes, and spiral prolong overcoat is equiped with cooling medium pipe, cooling medium pipe is corresponding with condensation straight tube is provided with cooling medium straight tube, be provided with spiral media pipe with spiral cold-finger is corresponding, cooling medium straight tube near phlegma liquid collecting cavity side is provided with cooling medium entrance, and the cooling medium straight tube near side, steam buffer chamber is provided with cooling medium outlet.

Description

Spiral white liquor distilling unit
Technical field
The utility model belongs to Brewing equipment technical field, is specifically related to a kind of spiral white liquor distilling unit.
Background technology
In traditional solid state fermentation liquor production, wine unstrained spirits ripe by fermentation adopts the mode of rice steamer bucket distillation to obtain white wine.White liquor distilling device generally comprises rice steamer bucket and condensing works, and wine unstrained spirits loads in rice steamer bucket by the mode of artificial loaded steamer, and the bottom of rice steamer bucket passes into vapor distillation.In the process of distillation, along with the continuous heating of steam, in rice steamer, wine unstrained spirits material temperature degree constantly raises, and makes to be contained in alcohol in wine unstrained spirits and fragrance component through overflash, condensation, revaporization, so repeatedly repeatedly, finally reaches that polycomponent is concentrated, the object of extraction.
Wine steam generally just simply realizes reclaiming by a prolong by existing white wine condenser, but so simple wine vapor-recovery unit organic efficiency is low, can waste a large amount of energy.Generally, in the condensing equipment that drinks is produced, there is no comparatively energy-conservation efficient condensing equipment again.
Summary of the invention
In view of this, the purpose of this utility model is to provide a kind of spiral white liquor distilling unit, can improve the condensation efficiency of wine steam.
For achieving the above object, the utility model provides following technical scheme:
A kind of spiral white liquor distilling unit, comprise rice steamer bucket and condenser, steam-pipe is adopted to be connected between described rice steamer bucket and condenser, described condenser comprises the steam buffer chamber being positioned at upper end and the phlegma liquid collecting cavity being positioned at lower end, condensing unit is provided with between described steam buffer chamber and described phlegma liquid collecting cavity, described steam-pipe is connected with described steam buffer chamber, and the bottom of described phlegma liquid collecting cavity is provided with phlegma drain pipe;
Described condensing unit comprises spiral prolong, described spiral prolong comprises the two condensation straight tubes be connected with phlegma liquid collecting cavity with described steam buffer chamber respectively, spiral cold-finger is connected with between two described condensation straight tubes, and described spiral prolong overcoat is equiped with cooling medium pipe, described cooling medium pipe is corresponding with described condensation straight tube is provided with cooling medium straight tube, correspondingly with described spiral cold-finger be provided with spiral media pipe, described cooling medium straight tube near described phlegma liquid collecting cavity side is provided with cooling medium entrance, described cooling medium straight tube near side, described steam buffer chamber is provided with cooling medium outlet.
Further, between described steam buffer chamber and described phlegma liquid collecting cavity, annular is laid with at least one circle condensing unit from outside to inside.
Further, each side enclosing the close described steam buffer chamber of described condensing unit is provided with cooling medium outlet coil pipe, is provided with cooling medium entrance coil pipe near the side of phlegma liquid collecting cavity, described cooling medium outlet coil pipe is connected with the described cooling medium straight tube near side, described steam buffer chamber, described cooling medium entrance coil pipe is connected with the described cooling medium straight tube near described phlegma liquid collecting cavity side, described cooling medium entrance is arranged on described cooling medium entrance coil pipe, and described cooling medium outlet is arranged on described cooling medium outlet coil pipe.
Further, enclose corresponding two cooling mediums arranged of described condensing unit and export between coil pipe with adjacent two and be provided with communicating pipe I, enclose between the corresponding two cooling medium entrance coil pipes arranged of described condensing unit be provided with communicating pipe II with adjacent two.
The beneficial effects of the utility model are:
Spiral white liquor distilling unit of the present utility model, by arranging condensing unit between the steam buffer chamber and phlegma liquid collecting cavity of condenser, and condensing unit is set to spiral prolong and is sleeved on the cooling medium pipe outside spiral prolong, pass into from steam buffer chamber to the wine steam that phlegma liquid collecting cavity flows in spiral prolong, the cooling medium flowed to steam buffer chamber from phlegma liquid collecting cavity is passed in cooling medium pipe, and utilize the condensation straight tube near steam buffer chamber tentatively to cool wine steam, utilizing spiral cold-finger, the wine steam degree of depth is cooled, the cooling of spiral cold-finger to wine steam provides sufficient cooling environment, namely spiral cold-finger can not only make the heat-conducting area of the condenser of equal height greatly increase, tube fluid can also be made to form turbulent flow, improve heat transfer efficiency, in addition, spiral cold-finger is compared with condensation straight tube, more be conducive to the phase-change heat transfer of wine vapor condensation, thus further improve condensation efficiency.
Accompanying drawing explanation
In order to make the purpose of this utility model, technical scheme and beneficial effect clearly, the utility model provides following accompanying drawing to be described:
Fig. 1 is the structural representation of the utility model spiral white liquor distilling unit embodiment;
Fig. 2 is the structural representation of condenser;
Fig. 3 is the A-A sectional view of Fig. 2;
Fig. 4 is the structural representation of the white liquor distilling system adopting the spiral white liquor distilling unit of the present embodiment.
Embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail, and to make those skilled in the art better can understand the utility model being implemented, but illustrated embodiment is not as to restriction of the present utility model.
As shown in Figure 1, be the structural representation of the utility model spiral white liquor distilling unit embodiment.The spiral white liquor distilling unit of the present embodiment, comprises rice steamer bucket 1 and condenser 3, adopts steam-pipe 4 to be connected between rice steamer bucket 1 and condenser 3.
Condenser 3 comprises the steam buffer chamber 7 being positioned at upper end and the phlegma liquid collecting cavity 8 being positioned at lower end, condensing unit is provided with between steam buffer chamber 7 and phlegma liquid collecting cavity 8, steam-pipe 4 is connected with steam buffer chamber 7, and the bottom of phlegma liquid collecting cavity 8 is provided with phlegma drain pipe 9.The condensing unit of the present embodiment comprises spiral prolong 10, spiral prolong 10 comprises the two condensation straight tubes 11 be connected with phlegma liquid collecting cavity 8 with steam buffer chamber 7 respectively, spiral cold-finger 12 is connected with between two condensation straight tubes 11, and spiral prolong 10 overcoat is equiped with cooling medium pipe 13, cooling medium pipe 13 is corresponding with condensation straight tube 11 is provided with cooling medium straight tube 14, correspondingly with spiral cold-finger 12 be provided with spiral media pipe 15, cooling medium straight tube 14 near phlegma liquid collecting cavity 8 side is provided with cooling medium entrance, cooling medium straight tube 14 near side, steam buffer chamber 7 is provided with cooling medium outlet.
The spiral white liquor distilling unit of the present embodiment, by arranging condensing unit between the steam buffer chamber 7 and phlegma liquid collecting cavity 8 of condenser 3, and the cooling medium pipe 13 condensing unit being set to spiral prolong 10 and being sleeved on outside spiral prolong, the wine steam flowed to from steam buffer chamber 7 to phlegma liquid collecting cavity 8 is passed in spiral prolong 10, the cooling medium flowed to from phlegma liquid collecting cavity 8 to steam buffer chamber 7 is passed in cooling medium pipe 13, and utilize the condensation straight tube 11 pairs of wine steam near steam buffer chamber 7 tentatively to cool, utilizing spiral cold-finger 12 pairs of wine steam degree of depth coolings, the cooling of spiral cold-finger 12 pairs of wine steam provides sufficient cooling environment, namely spiral cold-finger 12 can not only make the heat-conducting area of the condenser 3 of equal height greatly increase, tube fluid can also be made to form turbulent flow, improve heat transfer efficiency, in addition, spiral cold-finger 12 is compared with condensation straight tube 11, more be conducive to the phase-change heat transfer of wine vapor condensation, thus further improve condensation efficiency.
Further, between steam buffer chamber 7 and phlegma liquid collecting cavity 8, annular is laid with at least one circle condensing unit from outside to inside.Each circle condensing unit is provided with cooling medium outlet coil pipe 16, is provided with cooling medium entrance coil pipe 17 near the side of phlegma liquid collecting cavity 8 near the side in steam buffer chamber 7, cooling medium outlet coil pipe 16 is connected with the cooling medium straight tube 14 near side, steam buffer chamber 7, cooling medium entrance coil pipe 17 is connected with the cooling medium straight tube 14 near phlegma liquid collecting cavity 8 side, cooling medium entrance 18 is arranged on cooling medium entrance coil pipe 17, and cooling medium outlet 19 is arranged on cooling medium outlet coil pipe 16.Further, enclose corresponding two cooling mediums arranged of condensing unit and export between coil pipe 16 with adjacent two and be provided with communicating pipe I, enclose between the corresponding two cooling medium entrance coil pipes 17 arranged of condensing unit be provided with communicating pipe II 20 with adjacent two.As shown in Figure 3, between the steam buffer chamber 7 of the present embodiment and phlegma liquid collecting cavity 8, annular is laid with two circle condensing units from outside to inside, namely cooling medium outlet coil pipe 16 and cooling medium entrance coil pipe 17 are equipped with two, be set in outside the condensing unit of correspondence ring, in order to improve condensation efficiency, outer ring is provided with 6 condensing units, and inner ring is provided with 4 condensing units.By arranging cooling medium entrance coil pipe 17 and cooling medium outlet coil pipe 16, can facilitate and equably cooling medium be passed in cooling medium pipe 13, making each condensing unit have same condensing capacity.The cooling medium of the present embodiment adopts cold water, can realize the effect of wine vapor condensation.
As shown in Figure 4, for adopting the structural representation of the white liquor distilling system of the spiral white liquor distilling unit of the present embodiment.This white liquor distilling system also comprises condensation pond 2, and in condensation pond 2, annular is laid with at least one condenser 3, and rice steamer bucket 1 and condenser 3 one_to_one corresponding are arranged on outside condensation pond 2, and it is connected to be provided with steam-pipe 4 between rice steamer bucket 1 and corresponding condenser 3.Concrete, condenser 3 is set to two, corresponding, rice steamer bucket 1 also correspondence is set to two, and the bottom in condensation pond 2 is provided with water-in 5, and top is provided with water outlet 6, can realize the water cycle in condensation pond 2, ensures that the water temperature in condensation pond 2 meets service requirements.By arranging condensation pond 2, and be arranged in condensation pond 2 by uniform for condenser 3 annular, be arranged on outside condensation pond 2 by corresponding with condenser 3 for rice steamer bucket 1, a condenser 3 and rice steamer bucket 1 form a set of distillation unit, namely be set together in multiple distillation collection of units, be convenient to the centralized management of white liquor distilling, floor space is little, can be applicable to the demand of suitability for industrialized production.
This white liquor distilling system also comprises the lifting appliance arranged with rice steamer bucket 1 one_to_one corresponding, and lifting appliance comprises stand 21, and stand 21 is provided with the electric block 22 of the Zeng Gai for lifting rice steamer bucket, is provided with and is connected steel cable 23, handled easily between electric block 22 with rice steamer lid.
The above embodiment is only for absolutely proving the preferred embodiment that the utility model is lifted, and protection domain of the present utility model is not limited thereto.The equivalent alternative or conversion that those skilled in the art do on the utility model basis, all within protection domain of the present utility model.Protection domain of the present utility model is as the criterion with claims.

Claims (4)

1. a spiral white liquor distilling unit, comprise rice steamer bucket and condenser, steam-pipe is adopted to be connected between described rice steamer bucket and condenser, it is characterized in that: described condenser comprises the steam buffer chamber being positioned at upper end and the phlegma liquid collecting cavity being positioned at lower end, condensing unit is provided with between described steam buffer chamber and described phlegma liquid collecting cavity, described steam-pipe is connected with described steam buffer chamber, and the bottom of described phlegma liquid collecting cavity is provided with phlegma drain pipe;
Described condensing unit comprises spiral prolong, described spiral prolong comprises the two condensation straight tubes be connected with phlegma liquid collecting cavity with described steam buffer chamber respectively, spiral cold-finger is connected with between two described condensation straight tubes, and described spiral prolong overcoat is equiped with cooling medium pipe, described cooling medium pipe is corresponding with described condensation straight tube is provided with cooling medium straight tube, correspondingly with described spiral cold-finger be provided with spiral media pipe, described cooling medium straight tube near described phlegma liquid collecting cavity side is provided with cooling medium entrance, described cooling medium straight tube near side, described steam buffer chamber is provided with cooling medium outlet.
2. spiral white liquor distilling unit according to claim 1, is characterized in that: between described steam buffer chamber and described phlegma liquid collecting cavity, annular is laid with at least one circle condensing unit from outside to inside.
3. spiral white liquor distilling unit according to claim 2, it is characterized in that: each side enclosing the close described steam buffer chamber of described condensing unit is provided with cooling medium outlet coil pipe, cooling medium entrance coil pipe is provided with near the side of phlegma liquid collecting cavity, described cooling medium outlet coil pipe is connected with the described cooling medium straight tube near side, described steam buffer chamber, described cooling medium entrance coil pipe is connected with the described cooling medium straight tube near described phlegma liquid collecting cavity side, described cooling medium entrance is arranged on described cooling medium entrance coil pipe, described cooling medium outlet is arranged on described cooling medium outlet coil pipe.
4. spiral white liquor distilling unit according to claim 3, it is characterized in that: enclose corresponding two cooling mediums arranged of described condensing unit and export between coil pipe with adjacent two and be provided with communicating pipe I, enclose between the corresponding two cooling medium entrance coil pipes arranged of described condensing unit be provided with communicating pipe II with adjacent two.
CN201420522733.7U 2014-09-12 2014-09-12 Spiral white liquor distilling unit Expired - Fee Related CN204185461U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420522733.7U CN204185461U (en) 2014-09-12 2014-09-12 Spiral white liquor distilling unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420522733.7U CN204185461U (en) 2014-09-12 2014-09-12 Spiral white liquor distilling unit

Publications (1)

Publication Number Publication Date
CN204185461U true CN204185461U (en) 2015-03-04

Family

ID=52617473

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420522733.7U Expired - Fee Related CN204185461U (en) 2014-09-12 2014-09-12 Spiral white liquor distilling unit

Country Status (1)

Country Link
CN (1) CN204185461U (en)

Similar Documents

Publication Publication Date Title
CN101709221A (en) Novel coke powder cooling device
CN205011733U (en) Novel making wine equipment
CN204185465U (en) Spiral white liquor distilling system
CN201973774U (en) Solar superconduction geothermal heating system
CN103884098B (en) Waste heat recovery air source water heater
CN204185459U (en) For the Distallation systm of white liquor distilling
CN204185461U (en) Spiral white liquor distilling unit
CN103952280A (en) Liquor distilling condenser
CN104263610A (en) Spiral white spirit distillation unit
CN204185460U (en) For the spiral condenser of white liquor distilling
CN205223164U (en) Efficient making wine equipment
CN104263616A (en) Spiral condenser for liquor distillation
CN104263618A (en) Distillation unit for white wine distillation
CN203494188U (en) Double-effect concentrator
CN104403904A (en) Distilled system for liquor distillation
CN204185458U (en) For the distillation unit of white liquor distilling
CN204185454U (en) White liquor distilling device
CN204185466U (en) For the condenser of white liquor distilling
CN204185462U (en) For the condensing works of white liquor distilling
CN104263615A (en) Spiral liquor distillation system
CN204185464U (en) Efficient white liquor distilling unit
CN104263614A (en) High-efficiency closed white wine distillation system
CN104263622A (en) Condensing device for liquor distillation
CN204185453U (en) The white liquor distilling system of high effective sealing
CN102367995A (en) Heat-pipe vacuum pipe collector

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150304

Termination date: 20150912

EXPY Termination of patent right or utility model