CN202039054U - Split type liquor distiller - Google Patents

Split type liquor distiller Download PDF

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Publication number
CN202039054U
CN202039054U CN201120146419XU CN201120146419U CN202039054U CN 202039054 U CN202039054 U CN 202039054U CN 201120146419X U CN201120146419X U CN 201120146419XU CN 201120146419 U CN201120146419 U CN 201120146419U CN 202039054 U CN202039054 U CN 202039054U
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CN
China
Prior art keywords
rice steamer
steamer bucket
bucket
lower floor
upper strata
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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
CN201120146419XU
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Chinese (zh)
Inventor
季良威
李平
王领
钟秀训
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Sichuan Yinfan Biotechnology Co Ltd
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Sichuan Yinfan Biotechnology Co Ltd
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Priority to CN201120146419XU priority Critical patent/CN202039054U/en
Application granted granted Critical
Publication of CN202039054U publication Critical patent/CN202039054U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses a split type liquor distiller, which comprises a rice steamer cover, a rice steamer barrel, a bottom boiler and rice steamer grates. The rice steamer barrel comprises an upper-layer rice steamer barrel and a lower-layer rice steamer barrel, and a sealing gasket is arranged at the position where the upper-layer rice steamer barrel is connected with the lower-layer rice steamer barrel. The bottoms of the upper-layer rice steamer barrel and the lower-layer rice steamer layer are both provided with rice steamer grates, and each rice steamer grate is formed by connecting two semicircular rice steamer grate bodies. The split type liquor distiller can sufficiently extract the available flavoring component from fermented grains, thereby improving liquor yield and finished product ratio, and reducing labor intensity of workers.

Description

Split type white spirit distiller
Technical field
The utility model relates to a kind of distillation plant of drinks, relates in particular to a kind of split type white spirit distiller that improves the yield of liquor and yield rate.
Background technology
In the prior art, produce the used water distilling apparatus of liquor and comprise wine rice steamer bucket, the flat rice steamer that is positioned at this barrel inner bottom part is combed and support wine rice steamer bucket, end pot one end of rice steamer bucket is connected with wine rice steamer bucket, another termination steam-pipe, valve is housed on the vapour pipe, be installed in the common Zeng Gai at wine rice steamer bucket top, one end communicates with wine rice steamer bucket, and be connected with the rice steamer tops, the other end is communicated with by airway with the condenser of collecting product, the condenser that is installed separately with the rice steamer bucket, collect the collection device of wine, the pipeline of eliminating waste liquid and control device thereof etc.Its working process is: when steam by valve and pipeline, when entering in end pot and the rice steamer bucket, the fermented mash in it is heated and isolates alcohol, the liquor that is distilled out is introduced the independent condenser that is provided with through airway and is cooled into wine liquid and flows into the liquor collection device.
In order to adapt to the large-scale production of traditional liquor; the movable rice steamer of many big-and-middle-sized wine enterprise's employing flipovers, fluid pressure type live body distilling machinery, station dial rice steamer; adopt aforementioned manner to reduce labour intensity; improved production efficiency; solved part mechanize problem in the liquor production process; but do not have solution for the yield of liquor that occurs in the still-process and the low problem of yield rate; major cause is as follows: one, traditional liquor is; just cover Zeng Gai when above the unstrained spirits layer, having occurred white vaporific fume, can lose part alcohol.Two, during traditional liquor, the rice steamer body is an individual layer, and the unstrained spirits layer is blocked up, is unfavorable for the vapour-liquid of mass transfer process exchange in the unstrained spirits layer in the rice steamer bucket, make alcohol residue losing after distillation poor in.Three, on traditional liquor during rice steamer, excessive because of labour intensity, the operational difference of workman can not guarantee the main points of " pine, light, accurate, thin, even, flat " of unstrained spirits material, can not accomplish slow fire distillation when steaming wine fully, also can make alcohol residue lose poor in.Four, traditional device for wine distilling Zeng Gai, rice steamer body all adopt water seal with linking of end pot, and rice steamer bucket pressure causes wine vapour to pass water seal and leaks generally at 0.02-0.05Mpa in steaming the wine process, causes serious wine to decrease.Five, traditional rice steamer bucket is when steaming wine, and fume can produce " wall effect " in mass transfer process, also can produce wine and decrease.
And, some terms of settlement have been proposed in existing patented technology for the yield of liquor and the low problem of yield rate, comprise the naturally cooling that uses monoblock type rice steamer bucket or condenser and Zeng Gai device as one.China Patent No. " 200920303178.8 " " improving the equipment of white liquor distilling Titian rate and the yield of liquor " of proposing for another example, it comprises rice steamer bucket, Zeng Gai, crosses device of air and condenser, be provided with tightness system between described rice steamer bucket and rice steamer lid, also be connected with a filtration unit between Zeng Gai and condenser, filtration unit is provided with valve and medium tube, and filtration medium is filled in the medium tube.Aforementioned techniques all is intended to solve the problem of the yield of liquor and yield rate, but inconvenience is arranged in actual mechanical process, can not well solve the problem of the yield of liquor and yield rate.Thereby existing patent avoid wine to decrease in sealing measure aspect obvious advantage is arranged, but there is not the improvement of essence at the great disadvantage of traditional liquor distiller, especially the liquor yield rate is low, and fermented mash is in still-process, and the unsettled situation of quality of white spirit is not taken on a new look yet.
Summary of the invention
The purpose of this utility model is to overcome the problems referred to above that existing white liquor distilling device exists, a kind of split type white spirit distiller is provided, adopt the utility model can fully extract available flavour ingredient in the poor unstrained spirits, thereby improve the yield of liquor and yield rate, and can reduce working strength of workers.
For achieving the above object, the technical solution adopted in the utility model is as follows:
A kind of split type white spirit distiller, comprise Zeng Gai, rice steamer bucket, end pot and rice steamer comb, it is characterized in that: described rice steamer bucket comprises upper strata rice steamer bucket and lower floor's rice steamer bucket, the junction of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with gasket seal, the bottom of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with rice steamer and combs, and described rice steamer comb is connected to form by the rice steamer comb body of two semicirculars in shape.
Described two rice steamer comb bodies are connected to form rice steamer by loose-leaf and comb, and rice steamer is combed and is connected by the Zeng Bi of removable pin with the rice steamer bucket.
Be provided with zigzag brine collecting ring on the top Zeng Bi of described upper strata rice steamer bucket and lower floor's rice steamer bucket.
Described brine collecting ring is welded on the Zeng Bi, and zigzag angle is 60 degree.
The junction of described upper strata rice steamer bucket and Zeng Gai is provided with gasket seal, and the junction of lower floor's rice steamer bucket and end pot is provided with gasket seal.
Adopt advantage of the present utility model to be:
One, rice steamer bucket of the present utility model comprises upper strata rice steamer bucket and lower floor's rice steamer bucket, the rice steamer bucket is divided into two-layer up and down, and be welded with the zig-zag brine collecting ring at two-layer top Zeng Bi up and down, especially be the best with 60 ° of zig-zag brine collecting rings, can effectively prevent wall effect, two-layer rice steamer bucket can make poor unstrained spirits more loose simultaneously, further improves the yield of liquor and yield rate.
Two, the utility model Zeng Gai and rice steamer bucket two portions comprise that the sealing of lower floor's rice steamer bucket and end pot all adopts gasket seal, are the best with the 20mm silica gel pad especially, can avoid fume to leak after compressing.
Three, the bottom of upper strata of the present utility model rice steamer bucket and lower floor rice steamer bucket all is provided with two semicircle rice steamers that are connected by loose-leaf and combs and the removable pin that it is connected with Zeng Bi, this structure can use driving that upper strata rice steamer bucket is sling after single flash finishes, extract removable pin out and will lose poor pouring out in the rice steamer bucket of upper strata, thereby the minimizing labor strength, the operation of lower floor's rice steamer bucket is identical with upper strata rice steamer bucket.
Four, behind employing the utility model, can make the main flavour ingredient extraction yield increase by 5-12% of liquor in the fermented mash.
Description of drawings
Fig. 1 is the utility model structural representation
Fig. 2 rotates the partial enlarged drawing of loose joint place for Fig. 1 medi-spring
Be labeled as among the figure: 1, coiled pipe cooler, 2, Zeng Gai, 3, brine collecting ring, 4, gasket seal, 5, upper strata rice steamer bucket, 6, thermal insulation layer, 7, lower floor's rice steamer bucket, 8, inner pot body, 9, the external jacket heating member, 10, end pot liquidometer, 11, cold pot water water intaking valve, 12, the chuck vent valve, 13, bottom valve, 14, the coil pipe vent valve, 15, cold pot water outlet valve, 16, the coil pipe intake valve, 17, the chuck intake valve, 18, removable pin, 19, flowing water Valve, 20, inlet valve, 21, distribution piping, 22, loose-leaf, 23, rice steamer is combed, and 24, end pot heating coil, 25, return line, 26, interchanger, 27, airway, 28, spring rotates loose joint, 29, loose joint is rotated in external reflux, 30, internal reflux water of condensation water inlet loose joint, 31, internal reflux water of condensation water outlet loose joint.
Embodiment
A kind of split type white spirit distiller, comprise Zeng Gai, rice steamer bucket, end pot and rice steamer comb, described rice steamer bucket comprises upper strata rice steamer bucket and lower floor's rice steamer bucket, the junction of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with gasket seal, the bottom of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with rice steamer and combs, and described rice steamer comb is connected to form by the rice steamer comb body of two semicirculars in shape.
Preferred implementation of the present utility model is, described two rice steamer comb bodies are connected to form rice steamer by loose-leaf and comb, and rice steamer is combed and is connected by the Zeng Bi of removable pin with the rice steamer bucket.
Another preferred implementation of the present utility model is, is provided with zigzag brine collecting ring on the top Zeng Bi of described upper strata rice steamer bucket and lower floor's rice steamer bucket, is provided with thermal insulation layer on the outer wall of described upper strata rice steamer bucket and lower floor's rice steamer bucket.
Further, described brine collecting ring is welded on the Zeng Bi, and zigzag angle is that 60 degree are best.
Another preferred implementation of the present utility model is, the junction of described upper strata rice steamer bucket and Zeng Gai is provided with gasket seal, and the junction of lower floor's rice steamer bucket and end pot is provided with gasket seal.
Below the utility model do is launched explanation:
Be provided with coiled pipe cooler in the utility model rice steamer lid, described coiled pipe cooler top is connected with water inlet pipe, and the bottom is connected with rising pipe, and water inlet pipe is provided with inlet valve, and rising pipe is provided with flowing water Valve.
Preferred implementation of the present utility model is that described coiled pipe cooler is down turriform.
Another preferred implementation of the present utility model is evenly to be provided with the flow guide bar of indentation under the coil pipe of described coiled pipe cooler.
The utility model also comprises reflux, described reflux comprises interchanger and distribution piping, interchanger one end is by airway and rice steamer lid internal communication, and the other end is communicated with distribution piping by return line, and distribution piping is arranged between upper strata rice steamer bucket and the lower floor's rice steamer bucket and is positioned at rice steamer comb below, upper strata.
Another preferred implementation of the present utility model is, described interchanger top is provided with flange, and flange is provided with spring and rotates loose joint, and spring rotates loose joint and is connected with airway, and spring rotation loose joint is connected with Zeng Gai by airway.
Further preferred, described return line also is connected with the feed supplement pipe.Described distribution piping is the cruciform distribution piping.
Another preferred implementation of the present utility model is, pot of the described end comprises inner pot body and external jacket heating member, with on the drainage conduit that inner pot body is communicated with bottom valve is set, the external jacket heating member has chuck intake valve, chuck vent valve, cold pot water water intaking valve and cold pot of water outlet valve by pipe connection respectively.
Further, be provided with end pot heating coil in the described inner pot body, end pot heating coil one end has the coil pipe intake valve by pipe connection, and the other end has the coil pipe vent valve by pipe connection.
Working process behind employing the utility model is as follows:
At first the gasket seal 4 of lower floor is put well, is inserted removable pin 18 that rice steamer combs and insert and good loose-leaf 22 is closed up, by driving with the fermented mash lower floor's rice steamer body 7 of packing into; Put the gasket seal 4 on upper strata well rice steamer comb removable pin and insert and good loose-leaf to be closed up, again by driving with the fermented mash upper strata rice steamer body 5 of packing into.Gasket seal 4 is put well, rice steamer lid 2 is rotated pivoted arms that loose joint 28 forms by spring to be forwarded on the rice steamer body and builds Zeng Gai, by pressure arm Zeng Gai and rice steamer body portion are compressed, loose joint 29, internal reflux water of condensation water inlet loose joint 30 is rotated in external reflux be connected with the rice steamer body with internal reflux water of condensation water outlet loose joint 31, and the injection water seal.Because it is more to add liquid in the fermenting process, charging finishes, and liquid has flooded end pot heating coil 24 in the inner bottom pot 8 of back.Open the inlet valve 20 of the coiled pipe cooler 1 of Zeng Gai, flowing water Valve 19 and interchanger water intaking valve, outlet valve, open fermentation groove liquid heating in the pot at the bottom of 16 pairs of chuck intake valve 17 and the coil pipe intake valves, beginning steam enters the poor unstrained spirits of lower floor's rice steamer body behind 10-15min, and in poor unstrained spirits, carry out the vapour-liquid exchange, liquid passes back in the poor unstrained spirits after fragrance matter extracts in the poor unstrained spirits by the zig-zag brine collecting ring 3 that is welded on the Zeng Bi, steam enters and carries out the vapour-liquid exchange in the poor unstrained spirits in upper strata, and liquid is gone up the zig-zag brine collecting ring and passed back in the poor unstrained spirits fragrance matter in the poor unstrained spirits is extracted by being welded on Zeng Bi.The higher alcohol steam of concentration continues to rise, and arrives at coiled pipe cooler 1 and alcohol steam is partly cooled back to flow in the poor unstrained spirits the poor unstrained spirits in upper strata is extracted once more, also the poor unstrained spirits of lower floor is extracted simultaneously; The remaining part alcohol steam cools off through interchanger, passes back into lower floor rice steamer body top through return line 25 again, and the cruciform distribution piping 21 that is evenly distributed with 2-3mm hole by the below is sprayed in the poor unstrained spirits of lower floor, and the poor unstrained spirits of lower floor is extracted once more.Backflow 30-40min begins liquor later, the liquid level that distillatory is observed in the end pots by end pot liquidometer 10 simultaneously, and end pot liquid level should remain near the liquidometer supporting tube in 30-45min, and keeps liquid level by the additional at any time arrack of return line 25 at any time.After distillation finished, closed clip cover intake valve 17 and coil pipe intake valve 16 were opened chuck vent valve 12 and coil pipe vent valve 14 with residue vapor emptying in the rice steamer; Close chuck vent valve 12, open cold pot water water intaking valve 11 and cold pot water outlet valve 15, carry out cold pot.The spring of taking rice steamer lid water intaking valve, outlet valve and external reflux pipe apart rotates loose joint, liquid is chilled to room temperature substantially in the end this moment pot, trip spring rotates the pivoted arm screw of loose joint, the rice steamer cover tape is risen and rotate out, unclamping upper strata removable pin utilization driving hangs out upper strata rice steamer bucket and will lose the poor specified location of pouring into, lower floor's rice steamer bucket operation is the same, by bottom valve 13 material in the end pot is emitted standby aftertreatment, the single flash end of processing.
More than be preferred implementation of the present utility model, thereby protection domain of the present utility model is not limited to above-mentioned record, those skilled in the art can also make some distortion according to above-mentioned record, and these distortion all should be considered as protection domain of the present utility model.

Claims (5)

1. split type white spirit distiller, comprise Zeng Gai, rice steamer bucket, end pot and rice steamer comb, it is characterized in that: described rice steamer bucket comprises upper strata rice steamer bucket and lower floor's rice steamer bucket, the junction of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with gasket seal, the bottom of upper strata rice steamer bucket and lower floor's rice steamer bucket is provided with rice steamer and combs, and described rice steamer comb is connected to form by the rice steamer comb body of two semicirculars in shape.
2. split type white spirit distiller according to claim 1 is characterized in that: described two rice steamer comb bodies are connected to form rice steamer by loose-leaf and comb, and rice steamer is combed and is connected by the Zeng Bi of removable pin with the rice steamer bucket.
3. split type white spirit distiller according to claim 1 and 2 is characterized in that: be provided with zigzag brine collecting ring on the top Zeng Bi of described upper strata rice steamer bucket and lower floor's rice steamer bucket.
4. split type white spirit distiller according to claim 3 is characterized in that: described brine collecting ring is welded on the Zeng Bi, and zigzag angle is 60 degree.
5. split type white spirit distiller according to claim 3 is characterized in that: the junction of described upper strata rice steamer bucket and Zeng Gai is provided with gasket seal, and the junction of lower floor's rice steamer bucket and end pot is provided with gasket seal.
CN201120146419XU 2011-05-10 2011-05-10 Split type liquor distiller Expired - Fee Related CN202039054U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201120146419XU CN202039054U (en) 2011-05-10 2011-05-10 Split type liquor distiller

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Application Number Priority Date Filing Date Title
CN201120146419XU CN202039054U (en) 2011-05-10 2011-05-10 Split type liquor distiller

Publications (1)

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CN202039054U true CN202039054U (en) 2011-11-16

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107964486A (en) * 2016-10-19 2018-04-27 南京九溪生物科技有限公司 The distillation equipment of small brewing device
CN108239589A (en) * 2018-01-15 2018-07-03 沈墅 A kind of liquid ethanol extracts collection system
CN110305762A (en) * 2019-08-01 2019-10-08 北京工商大学 A kind of solid state fermentation wine distiller
CN115537282A (en) * 2022-09-30 2022-12-30 贵州董酒股份有限公司 Production equipment of Dong fragrant type white spirit

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107964486A (en) * 2016-10-19 2018-04-27 南京九溪生物科技有限公司 The distillation equipment of small brewing device
CN108239589A (en) * 2018-01-15 2018-07-03 沈墅 A kind of liquid ethanol extracts collection system
CN110305762A (en) * 2019-08-01 2019-10-08 北京工商大学 A kind of solid state fermentation wine distiller
CN115537282A (en) * 2022-09-30 2022-12-30 贵州董酒股份有限公司 Production equipment of Dong fragrant type white spirit

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

Granted publication date: 20111116

Termination date: 20170510