CN207041944U - A kind of distilling apparatus - Google Patents
A kind of distilling apparatus Download PDFInfo
- Publication number
- CN207041944U CN207041944U CN201720972323.6U CN201720972323U CN207041944U CN 207041944 U CN207041944 U CN 207041944U CN 201720972323 U CN201720972323 U CN 201720972323U CN 207041944 U CN207041944 U CN 207041944U
- Authority
- CN
- China
- Prior art keywords
- filtering tank
- evaporator
- drainer
- steam
- cooling water
- 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
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A kind of distilling apparatus provided by the utility model includes evaporator, first distillation steam pipe road, after-fractionating steam pipe road and condensation component, the condensation component includes filtering tank, cooling water pipe and drainer, evaporator and the filtering tank described in the first distillation vapour pipeline communication, filtering tank and the drainer described in the after-fractionating vapour pipeline communication, the filtering tank includes filter house and cooling end, the filter house is arranged at the lower section of the cooling end, the cooling water pipe connects the cooling end of the filtering tank and the drainer respectively, the evaporator is provided with evaporation cavity, steam inlet and materail tube, steam is able to enter the evaporation cavity by the steam inlet, the materail tube connects the filter house of the filtering tank and the evaporator.So as to be distilled by steam-heated mode, hops oil product is prepared to replace odor type pellet hop to be added directly into boiling pot, whirlpool stillpot even zymotic fluid, to increase the fragrance of beer.
Description
Technical field
Brewage field is the utility model is related to, is a kind of distillation dress suitable for hop components extraction specifically
Put.
Background technology
The production technology of beer generally comprise the crushing of malt, gelatinization, saccharification, filter, boil, precipitation of circling round, fermentation with
And ripe packaging, bitter type hops and aroma hops are typically added portionwise in boiling part, it is tasty and refreshing that hops can assign beer
Bitter taste and distinctive fragrance, promote protein coagulating, improve the non-biostability of beer, also help beer foam and rise
To bacteriostasis.Hops most important composition in the brewing process of beer is hop resin, hop oil and polyphenol substance, beer
Bitter taste essentially from hop resin, isomery alpha-acid therein, there is strong bitter taste and antiseptic power, the bubble of beer can be increased
Foam stability, by directly adding hops to boiling pot, the utilization rate of isomery alpha-acid causes the waste of hops less than 10%
Use.
The main component to be worked in hop oil is terpenes hydrocarbon, and its volatility is stronger, even if at normal temperatures
Can volatilization, there is more than 90% to be evaporated in Wort boiling, cooling, fermentation process, be dissolved in beer only 8%~
9%, the Wort boiling time is longer, and loss is more, and just because of this, the method that hops are added using gradation, purpose is also that
Retain appropriate hop oil, to protrude the hops of beer perfume, thus, relevant manufacturer needs research and development hops oil product badly to replace perfume
Type pellet hop.
Utility model content
Main purpose of the present utility model is to provide a kind of distilling apparatus, its overcome the deficiencies in the prior art, passes through steaming
The mode of vapour heating distillation, prepares hops oil product to replace odor type pellet hop to be added directly into boiling pot, whirlpool stillpot
Even in zymotic fluid, to increase the fragrance of beer.
Another object of the present utility model is to provide a kind of distilling apparatus, and it is progressively cooled down by way of multistage cools down
Retort gas, volatile hops oil ingredient is condensed, for hops oil product is made.
To achieve the above objectives, the technical solution adopted in the utility model is：A kind of distilling apparatus includes evaporator, first
Steam pipe road, after-fractionating steam pipe road and condensation component are distilled, the condensation component includes filtering tank, cooling water pipe and condensation
Tank, evaporator and the filtering tank described in the first distillation vapour pipeline communication, mistake described in the after-fractionating vapour pipeline communication
Filter tank and the drainer, the filtering tank include filter house and cooling end, and the filter house is arranged at the cooling end
Lower section, the cooling water pipe connect the cooling end of the filtering tank and the drainer respectively, the evaporator be provided with evaporation cavity,
Steam inlet and materail tube, steam are able to enter the evaporation cavity by the steam inlet, described in the materail tube connection
The filter house of filtering tank and the evaporator.
According to an embodiment of the present utility model, the drainer is provided with condenser pipe, cold water cavity, upper perforated plate, lower perforated plate, steaming
Distillate outlet and the second cooling water outlet pipe, the condenser pipe compartment of terrain penetrate the upper perforated plate and lower perforated plate, the cold water
Chamber is formed between the upper perforated plate and the lower perforated plate, and the cold water cavity connects the cooling water pipe and second cooling water
Outlet pipe, the distillate outlet connect the lower end of the drainer.
According to an embodiment of the present utility model, the condenser pipe is provided with tilt outlet, and the tilt outlet is arranged at two
The condenser pipe lower end of side.
According to an embodiment of the present utility model, the filter house is provided with filtration members, and the filtration members compartment of terrain is uniformly arranged
Row, the filter house include CIP inlet pipes, and each CIP inlet pipes are towards each filtration members.
According to an embodiment of the present utility model, the evaporator further comprises tank body and stirring parts, the evaporation
Chamber is formed in the tank body, and the stirring parts include control unit, drive rod and mixing part, and the drive rod can drivingly connect
The control unit and the mixing part are connect, the mixing part is rotatably installed in the tank body, and the control unit is installed on
Outside the tank body.
Brief description of the drawings
Fig. 1 is the structural representation according to the distilling apparatus of a preferred embodiment of the present utility model.
Fig. 2 is the structural representation according to the drainer of above preferred embodiment of the present utility model.
Embodiment
Describe to be used to disclose the utility model so that those skilled in the art can realize the utility model below.Retouch below
Preferred embodiment in stating is only used as illustrating, it may occur to persons skilled in the art that other obvious modifications.
As shown in Figure 1 to Figure 2 be a kind of distilling apparatus, the distilling apparatus includes evaporator 10, first and distills steam pipe
Road 21, after-fractionating steam pipe road 22 and condensation component 30, it is described condensation component 30 include filtering tank 31, cooling water pipe 32 and
Drainer 33, the first distillation steam pipe road 21 connect the evaporator 10 and the filtering tank 31, the after-fractionating steam pipe
Road 22 connects the filtering tank 31 and the drainer 33, and the filtering tank 31 includes filter house 311 and cooling end 313, institute
The lower section that filter house 311 is arranged at the cooling end 313 is stated, the cooling water pipe 32 connects the cooling of the filtering tank 31 respectively
Portion 313 and the drainer 33 so that cooling water respectively from the lower section of the cooling end 313 and the drainer 33 enter again from
Top is flowed out, and the evaporator 10 is provided with evaporation cavity 100, steam inlet 101 and materail tube 104, and steam is able to by described
Steam inlet 101 enters the evaporation cavity 100, is able to heat the material in the evaporation cavity 100, the materail tube
The filter house 311 and the evaporator 10 of the 104 connection filtering tanks 31, filter material and foreign objects in the filtering tank 31
Material is able to enter in the evaporation cavity 100 by the materail tube 104, so as to by way of steam heating distillation, prepare wine
Caul-fat product replaces the odor type pellet hop to be added directly into boiling pot, whirlpool stillpot even in zymotic fluid, to increase beer
Fragrance.
The drainer 33 is provided with condenser pipe 331, cold water cavity 332, upper perforated plate 333, lower perforated plate 334, distillate outlet
336 and the second cooling water outlet pipe, the compartment of terrain of condenser pipe 331 penetrates the upper perforated plate 333 and lower perforated plate 334, described cold
Water cavity 332 is formed between the upper perforated plate 333 and the lower perforated plate 334, and the cold water cavity 332 connects the cooling water pipe 32
With second cooling water outlet tube 337, the cooling water pipe 32 is arranged on the downside of the condenser pipe 331 of side, and described second
Cooling water outlet tube 337 is arranged at the upside of the condenser pipe 331 of opposite side, and cooling water enters described cold from the cooling water pipe 32
Water cavity 332, then second cooling water outlet tube 337 above opposite side flow out, effectively to the steaming in the condenser pipe 331
Evaporate vapour to be condensed, the distillate outlet 336 connects the lower end of the drainer 33, is able to collect distillate.
Wherein, the condenser pipe 331 is provided with tilt outlet 335, and the tilt outlet 335 is arranged at the condensation of both sides
The lower end of pipe 331, it is easy to collect distillate.
Wherein, the drainer 33 is in fusiformis structure, is advantageous to distill entrance and the centralized collection of distillate of vapour.
The filter house 311 is provided with filtration members 314, and the compartment of terrain of filtration members 314 is evenly distributed, the filter house 311
Including CIP inlet pipes 312, each CIP inlet pipes 312 are able to enter the filtration members 314 towards each filtration members 314
Row effectively cleans.
Wherein, the cooling end 313 includes the first cooling water outlet tube 315, is connected to the cooling water pipe of the cooling end 313
32 are located at the both sides of the filtering tank 31, the cooling water of cooling water from below with first cooling water outlet tube 315 respectively
Pipe 32 enters the cooling end 313 of the filtering tank 31, then is flowed out from first cooling water outlet tube 315 of top.
The evaporator 10 is further provided with outlet of sewer 102 and condensation-water drain 103, the He of outlet of sewer 102
The condensation-water drain 103 is located at the both sides of the evaporator 10 respectively, is respectively communicated with the bottom of the evaporator 10, is entered
The effective blowdown of row.
Wherein, the evaporator 10 further comprises tank body 11, supporting part 12 and stirring parts 13, and the supporting part 12 is pacified
Loaded on the downside of the tank body 11, the supporting part 12 for jet chimney, sewage conduct and condensing water conduit arrangement and
Connection, the tank body 11 include coning tower tray portion 111, expansion section 112, elongate portion 113 and evaporation part 114, the elongate portion 113 from
The evaporation part 114 upwardly extends, coning tower tray portion 111 and the elongate portion 113 described in the integrally connected of expansion section 112, described
Coning tower tray portion 111 is located at the upper end of the tank body 11, and the coning tower tray portion 111 is upward tapered configuration, be advantageous to distill vapour jet flow to
The first distillation steam pipe road 21.
The stirring parts 13 include control unit 131, drive rod 132 and mixing part 133, and the drive rod 132 connects institute
Control unit 131 and the mixing part 133 are stated, the mixing part 133 is rotatably installed on the evaporation cavity 100 of the tank body 11
Interior, the control unit 131 is installed on outside the tank body 11, by the operation of the control unit 131, is able to drive the drive rod
132, to drive the mixing part 133 to be stirred the material in the evaporation cavity 100.
In use, extraneous hops material is entered in the evaporator 10 by the materail tube 104, then pass through the steaming
Vapor inlet 101 is passed through vapor, and the stirring parts 13 persistently stir material, vapour will be distilled caused by liquid boiling and import described the
One distillation vapour inlet pipe, then import in the connected filtering tank 31, the filter house 311 carries out layering, mistake to distillation vapour
Material after filter can be reclaimed by the materail tube 104 to be entered in the evaporator 10, the waste of material is effectively prevented, after filtering
Distillation vapour be upwardly into the cooling end 313, the after-fractionating steam pipe road 22 is imported after cooling again, enters back into connected institute
State drainer 33, the cooling water in the cooling chamber is able to effectively cool to the condenser pipe 331 so that the condensation
Distillation vapour in pipe 331 is condensed into liquid, then is collected by the distillate outlet 336.So as to be cooled down by multistage
Mode progressively cool down retort gas, condense volatile hops oil ingredient, for hops oil products is made, while pass through steaming
Vapour heating need not use other solvents beyond system components, and guarantee will not introduce new impurity.
The advantages of general principle of the present utility model, principal character and the utility model has been shown and described above.One's own profession
The technical staff of industry is it should be appreciated that the utility model is not restricted to the described embodiments, described in above-described embodiment and specification
Simply principle of the present utility model, the utility model also has respectively on the premise of the spirit and scope of the utility model is not departed from
Kind changes and improvements, these changes and improvements are both fallen within claimed the scope of the utility model.The requires of the utility model
Protection domain defined by appended claims and its equivalent.
Claims (5)
1. a kind of distilling apparatus, it is characterised in that including evaporator, the first distillation steam pipe road, after-fractionating steam pipe road and cold
Solidifying component, the condensation component include filtering tank, cooling water pipe and drainer, steaming described in the first distillation vapour pipeline communication
Tank and the filtering tank are sent out, filtering tank and the drainer, the filtering tank include described in the after-fractionating vapour pipeline communication
Filter house and cooling end, the filter house are arranged at the lower section of the cooling end, and the cooling water pipe connects the mistake respectively
The cooling end of filter tank and the drainer, the evaporator are provided with evaporation cavity, steam inlet and materail tube, and steam is passed through
The steam inlet enters the evaporation cavity, and the materail tube connects the filter house of the filtering tank and the evaporator.
2. distilling apparatus according to claim 1, it is characterised in that the drainer is provided with condenser pipe, cold water cavity, upper tube
Plate, lower perforated plate, distillate outlet and the second cooling water outlet pipe, the condenser pipe compartment of terrain penetrate the upper perforated plate and down tube
Plate, the cold water cavity are formed between the upper perforated plate and the lower perforated plate, and the cold water cavity connects the cooling water pipe and institute
The second cooling water outlet tube is stated, the distillate outlet connects the lower end of the drainer.
3. distilling apparatus according to claim 2, it is characterised in that the condenser pipe is provided with tilt outlet, the inclination
Outlet is arranged at the condenser pipe lower end of both sides.
4. distilling apparatus according to claim 3, it is characterised in that the filter house is provided with filtration members, the filtration members
Compartment of terrain is evenly distributed, and the filter house includes CIP inlet pipes, and each CIP inlet pipes are towards each filtration members.
5. according to any described distilling apparatus in Claims 1 to 4, it is characterised in that the evaporator further comprises tank
Body and stirring parts, the evaporation cavity are formed in the tank body, and the stirring parts include control unit, drive rod and stirring
Portion, the drive rod can drivingly connect the control unit and the mixing part, and the mixing part is rotatably installed on described
In tank body, the control unit is installed on outside the tank body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720972323.6U CN207041944U (en) | 2017-08-04 | 2017-08-04 | A kind of distilling apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720972323.6U CN207041944U (en) | 2017-08-04 | 2017-08-04 | A kind of distilling apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207041944U true CN207041944U (en) | 2018-02-27 |
Family
ID=61498356
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720972323.6U Expired - Fee Related CN207041944U (en) | 2017-08-04 | 2017-08-04 | A kind of distilling apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207041944U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110129172A (en) * | 2019-06-11 | 2019-08-16 | 江西省农业科学院农产品质量安全与标准研究所 | Distiller and its distilling apparatus |
-
2017
- 2017-08-04 CN CN201720972323.6U patent/CN207041944U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110129172A (en) * | 2019-06-11 | 2019-08-16 | 江西省农业科学院农产品质量安全与标准研究所 | Distiller and its distilling apparatus |
| CN110129172B (en) * | 2019-06-11 | 2022-04-08 | 江西省农业科学院农产品质量安全与标准研究所 | Distiller and distilling device thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180227 Termination date: 20210804 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |