CN203174076U

CN203174076U - Distiller

Info

Publication number: CN203174076U
Application number: CN201320226433XU
Authority: CN
Inventors: 刘霞
Original assignee: Individual
Current assignee: Individual
Priority date: 2013-04-28
Filing date: 2013-04-28
Publication date: 2013-09-04
Anticipated expiration: 2023-04-28

Abstract

The utility model relates to a distiller, is particularly suitable for distilling brandy, and belongs to the technical field of distiller structures. The distiller comprises a first distillatory kettle which is provided with a heat device, a second distillatory kettle, a preheater which is arranged above the second distillatory kettle, and a foreshot condenser which is used for condensing mild wine gas, wherein the first distillatory kettle, the second distillatory kettle, the preheater and the foreshot condenser are communicated through pipelines which are provided with discharge valves; a first reflux device and a second reflux device are respectively arranged on the first distillatory kettle and the preheater; the first reflux device and the second reflux device are respectively communicated with the second distillatory kettle and the foreshot condenser through pipelines; a wine gas reflux pipe communicated with the second distillatory kettle is arranged in the preheater; the preheater is provided with a feed valve; a condenser which is used for condensing high wine gas is arranged below the foreshot condenser; and the condenser is provided with a wine tester and a water inlet valve. The distiller is reasonable in structure design and convenient to use, and can be used for producing raw brandy with alcoholic strength over 60 percent only in once distillation.

Description

Distiller

Technical field

The utility model relates to a kind of distiller, is specially adapted to the distillation of brandy, belongs to the distiller technical field of structures.

Background technology

Brandy is a kind of through distilling the wine of drinking that forms, existing brandy distillation plant is Charente kettle formula distiller, this distiller mainly is made up of still pot, preheater and condenser etc., complex structure, use inconvenience, need carry out twice distillation and just can make the original brandy of alcoholic strength more than 60%.

Summary of the invention

The purpose of this utility model is to solve the weak point that above-mentioned prior art exists, and a kind of reasonable in design is provided, and is easy to use, only carries out the distiller that single flash just can make alcoholic strength 60% above original brandy.

The utility model is achieved through the following technical solutions:

Distiller, it is characterized in that comprising first still pot 12 that first heating unit 14 is installed, the after-fractionating pot 33 of second heating unit 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, the foreshot's condenser 25 that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot 12, be separately installed with first return channel 4 on the preheater 20, second return channel 19, first return channel 4, second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return line 21 that communicates with after-fractionating pot 33 is installed in the preheater 20, feed valve 1 is installed on the preheater 20, the below of foreshot's condenser 25 is equipped with the condenser 28 for condensation height fume, is equipped with on the condenser 28 to survey drinking vessel 29 and water intaking valve 30;

Be connected by the pipeline that first baiting valve 6 is installed between described first still pot 12 and the preheater 20, this pipeline is provided with the branch line that is connected with after-fractionating pot 33, second baiting valve 7 is installed on this branch line, is connected by the liquid returning tube that valve 27 is installed between preheater 20 and the foreshot's condenser 25;

Described first return channel 4 is connected with after-fractionating pot 33 by first swan neck 3 that first valve 9 is installed, and second return channel 19 is connected with foreshot's condenser 25 by second swan neck 17;

On described first still pot 12 pressure release valve 8 is installed;

The outside of described foreshot's condenser 25 is equipped with spilling water valve 22, and inside is equipped with foreshot's prolong 24, and visor 23 is installed on foreshot's prolong 24;

Described first still pot 12 is separately installed with first wash water valve 15, second wash water valve 16 with the bottom of after-fractionating pot 33;

On described first return channel 4, second return channel 19, the condenser 28 thermometer is installed all;

The outside surface of described first still pot 12 and after-fractionating pot 33 is separately installed with first thermal insulation layer 13, second thermal insulation layer 31;

Described first still pot 12, after-fractionating pot 33, preheater 20 are separately installed with for first liquid level tube 10, second liquid level tube 11, the 3rd liquid level tube 2 that show liquid level.

Distiller structure design of the present utility model is reasonable in design, each parts is used, only carry out single flash and just can make alcoholic strength 60% above original brandy, fuel economy, improve wine efficient processed, in addition, owing to adopt foreshot's condenser, make the original brandy exquisiteness that makes, be continuous, the alcohol that has promoted wine liquid is just spent.

Description of drawings

Fig. 1: the structural representation of the utility model distiller.

Embodiment

Provide embodiment of the present utility model below with reference to accompanying drawing, be used for the utility model is described further.

Embodiment 1

The distiller of present embodiment, comprise first still pot 12 that first heating unit 14 is installed, the after-fractionating pot 33 of second heating unit 32 is installed, be installed on the preheater 20 of after-fractionating pot 33 tops, the foreshot's condenser 25 that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot 12, be separately installed with first return channel 4 on the preheater 20, second return channel 19, first return channel 4, second return channel 19 is respectively by pipeline and after-fractionating pot 33, foreshot's condenser 25 is connected, the fume return line 21 that communicates with after-fractionating pot 33 is installed in the preheater 20, feed valve 1 is installed on the preheater 20, the below of foreshot's condenser 25 is equipped with the condenser 28 for condensation height fume, is equipped with on the condenser 28 to survey drinking vessel 29 and water intaking valve 30; Be connected by the pipeline that first baiting valve 6 is installed between first still pot 12 and the preheater 20, this pipeline is provided with the branch line that is connected with after-fractionating pot 33, second baiting valve 7 is installed on this branch line, is connected by the liquid returning tube that valve 27 is installed between preheater 20 and the foreshot's condenser 25; First return channel 4 is connected with after-fractionating pot 33 by first swan neck 3 that first valve 9 is installed, and second return channel 19 is connected with foreshot's condenser 25 by second swan neck 17; On first still pot 12 pressure release valve 8 is installed; The outside of foreshot's condenser 25 is equipped with flowing water valve 22, and inside is equipped with foreshot's prolong 24, and visor 23 is installed on foreshot's prolong 24; First still pot 12 is separately installed with first wash water valve 15, second wash water valve 16 with the bottom of after-fractionating pot 33;

On first return channel 4, second return channel 19, the condenser 28 thermometer is installed all; The outside surface of first still pot 12 and after-fractionating pot 33 is separately installed with first thermal insulation layer 13, second thermal insulation layer 31;

First still pot 12, after-fractionating pot 33, preheater 20 are separately installed with for first liquid level tube 10, second liquid level tube 11, the 3rd liquid level tube 2 that show liquid level.

Wine principle processed: at first with pressure release valve 8, first baiting valve 6, second baiting valve 7 is opened, fermented liquid injects preheater 20 through feed valve 1, add to first still pot 12,75% of after-fractionating pot 33 capacity, close pressure release valve 8 and first baiting valve 6 then, second baiting valve 7, close feed valve 1 after the fermented liquid with preheater 20 injections 75% capacity again, open first valve 9, primary heater 14 and secondary heater 32 are connected, first thermometer 5 and second thermometer 18 are looked in sight, when temperature reaches 85 degrees centigrade, water intaking valve 30 and spilling water valve 22 are opened, the temperature of controlling the 3rd thermometer 26 is no more than 40 degrees centigrade, close the secondary heater 32 of after-fractionating pot 33, the wine vapour of first still pot 12 continues to be heated to out wine vapour with the fermented liquid in the after-fractionating pot 33, wine vapour slowly heats the fermented liquid in the preheater 20 through the wine vapour return line 21 of preheater 20 inside, wine vapour continues through second swan neck 17, enter foreshot's condenser 25, low alcohol vapour liquefies is easily had foreshot's prolong 24 of cold water to be condensed into wine liquid by inside, remain in foreshot's condenser 25 inside, height quality liquor vapour enters inside and has by pipe connecting in the spiral copper pipe in the condenser 28 of cold water, form wine liquid through condensation and enter survey drinking vessel 29, again wine liquid is inserted and contain drinking vessel, when first thermometer 5 reaches 100 degrees centigrade, open secondary heater 32, close primary heater 14 simultaneously, after-fractionating pot 33 continues distillation, at this moment open pressure release valve 8, the raffinate of first still pot, 12 inside is discharged by second wash water valve 16, by valve 27 the good fermented liquid of preheating in the wine liquid in foreshot's condenser 25 and the preheater 20 is injected in first still pot 12 again, again preheater 20 is injected a certain amount of fermented liquid, close secondary heater 32, open primary heater 14 simultaneously and continue distillation, circulation constantly is distilled to fermented liquid and uses up according to this, with finishing until distillation in the injection of the fermented liquid in the preheater 20 after-fractionating pot 33, open first wash water valve 15 for the last time, second wash water valve 16 and pressure release valve 8 drain raffinate.

Claims

1. distiller, it is characterized in that comprising first still pot (12) that first heating unit (14) is installed, the after-fractionating pot (33) of second heating unit (32) is installed, be installed on the preheater (20) of after-fractionating pot (33) top, the foreshot's condenser (25) that is used for the low fume of condensation, four are connected by the pipeline that baiting valve is installed, first still pot (12), be separately installed with first return channel (4) on the preheater (20), second return channel (19), first return channel (4), second return channel (19) is respectively by pipeline and after-fractionating pot (33), foreshot's condenser (25) is connected, the fume return line (21) that communicates with after-fractionating pot (33) is installed in the preheater (20), feed valve (1) is installed on the preheater (20), the below of foreshot's condenser (25) is equipped with the condenser (28) for condensation height fume, is equipped with on the condenser (28) to survey drinking vessel (29) and water intaking valve (30).

2. according to the described distiller of claim 1, it is characterized in that being connected by the pipeline that first baiting valve (6) is installed between described first still pot (12) and the preheater (20), this pipeline is provided with the branch line that is connected with after-fractionating pot (33), second baiting valve (7) is installed on this branch line, is connected by the liquid returning tube that valve (27) is installed between preheater (20) and the foreshot's condenser (25).

3. according to the described distiller of claim 1, it is characterized in that described first return channel (4) is connected with after-fractionating pot (33) by first swan neck (3) that first valve (9) is installed, second return channel (19) is connected with foreshot's condenser (25) by second swan neck (17).

4. according to the described distiller of claim 1, it is characterized in that being equipped with on described first still pot (12) pressure release valve (8).

5. according to the described distiller of claim 1, it is characterized in that the outside of described foreshot's condenser (25) is equipped with spilling water valve (22), inside is equipped with foreshot's prolong (24), and visor (23) is installed on foreshot's prolong (24).

6. according to the described distiller of claim 1, it is characterized in that described first still pot (12) and the bottom of after-fractionating pot (33) are separately installed with first wash water valve (15), second wash water valve (16).

7. according to the described distiller of claim 1, it is characterized in that described first return channel (4), second return channel (19), condenser all are equipped with thermometer on (28).

8. according to the described distiller of claim 1, it is characterized in that the outside surface of described first still pot (12) and after-fractionating pot (33) is separately installed with first thermal insulation layer (13), second thermal insulation layer (31).

9. according to the described distiller of claim 1, it is characterized in that described first still pot (12), after-fractionating pot (33), preheater (20) are separately installed with for first liquid level tube (10), second liquid level tube (11), the 3rd liquid level tube (2) that show liquid level.