CN217709377U

CN217709377U - Liquid distiller for high-degree white spirit

Info

Publication number: CN217709377U
Application number: CN202220230539.6U
Authority: CN
Inventors: 颜欣萍; 郑巧真; 叶云清; 颜文凤
Original assignee: Quanzhou Zhongxiang Biotechnology Co ltd
Current assignee: Quanzhou Zhongxiang Biotechnology Co ltd
Priority date: 2022-01-27
Filing date: 2022-01-27
Publication date: 2022-11-01
Anticipated expiration: 2032-01-27

Abstract

The utility model relates to a liquid distiller of high white spirit, including first stills, second stills, pre-heater and cooler, the end of giving vent to anger of first stills is connected through first connecting pipe with the inlet end of second stills, is equipped with wine gas conveyer pipe in the pre-heater, and the pre-heater is worn out and the cooler intercommunication to the one end of wine gas conveyer pipe, and the other end of wine gas conveyer pipe communicates with the end of giving vent to anger of second stills, and the pre-heater passes through unloading pipe and second stills intercommunication, is equipped with the wine liquid charging hole in the pre-heater. The utility model discloses, because wine gas cools down through the pre-heater earlier, can reduce the work energy consumption of cooler, utilize the heat of wine gas to heat the wine with dregs simultaneously, the wine with dregs passes through the unloading pipe and gets into second stills, can reduce second stills's energy consumption, through twice distillation, can promote alcohol concentration in the beverage.

Description

Liquid distiller for high-degree white spirit

Technical Field

The utility model relates to a high white spirit liquid distiller.

Background

In the process of making the high-alcohol white spirit, the fermented wine mash is distilled, so that ethanol and flavor components in the wine mash volatilize along with water vapor, and then the wine mash is cooled to form high-concentration wine. For example, in chinese utility model patent No. CN212152230U entitled "a white spirit distillation system", a white spirit distillation system is disclosed, which comprises a steam generator, a white spirit distiller and a white spirit cooler; adopt first steam delivery pipe between steam generator and the white spirit distiller, first steam delivery pipe is used for the leading-in white spirit distiller of high temperature steam that produces steam generator, adopt second steam delivery pipe to connect between white spirit distiller and the white spirit cooler, second steam delivery pipe is used for the leading-in white spirit cooler of the wine steam with the separation, the white spirit cooler is with the condensation of wine steam one-tenth white spirit wine.

According to the existing liquor distiller, the proportion of ethanol distilled from liquor in the liquor distiller is relatively low, so that the alcohol concentration of liquor is relatively low, and the residual liquor tailing in the liquor distiller is difficult to be fully utilized and directly discharged, thereby causing resource waste.

Accordingly, the present inventors have made extensive studies to solve the above problems and have made the present invention.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a can improve alcohol concentration in the beverage, more energy saving and consumption reduction's liquid distiller of high white spirit.

In order to achieve the above purpose, the utility model adopts the following technical scheme:

the utility model provides a high white spirit liquid distiller, includes first stills, second stills, pre-heater and cooler, the end of giving vent to anger of first stills is connected through first connecting tube with the inlet end of second stills, is equipped with the wine gas conveyer pipe in the pre-heater, the one end of wine gas conveyer pipe is worn out the pre-heater and is linked together with the cooler, the other end of wine gas conveyer pipe and the end intercommunication of giving vent to anger of second stills, the pre-heater passes through unloading pipe and second stills intercommunication, be equipped with the wine liquid charging hole in the pre-heater.

As the utility model discloses an optimal selection mode still includes the material pump, and the discharge gate of material pump passes through first conveying pipe and first stills intercommunication, and the feed inlet of material pump passes through the bottom intercommunication of second conveying pipe and second stills.

As the utility model discloses a preferred mode, be equipped with first control valve on the first conveying pipe, be equipped with the second control valve on the second conveying pipe, first conveying pipe still is equipped with the blow-off valve.

As the utility model discloses an preferred mode, first stills's lower extreme still is equipped with row material pipe, arranges to be equipped with the third control valve on the material pipe, arrange the one end of material pipe with first stills's lower extreme intercommunication, the other end with the feed inlet intercommunication of material pump.

As the utility model discloses an preferred mode, be equipped with first condenser in the pre-heater, first condenser has the setting and is in the delivery path of wine gas conveyer pipe and with the first condensing channel of wine gas conveyer pipe intercommunication.

As the preferred mode of the utility model, be equipped with the second condenser in the cooler, the second condenser has the setting and is in the delivery path of wine gas conveyer pipe and with the second condensation duct of wine gas conveyer pipe intercommunication.

As a preferable mode of the present invention, a cooling coil is further provided in the cooler.

As the utility model discloses an preferred mode, the top of pre-heater is equipped with the demister, wine gas delivery pipe extends to the upper portion of demister, the demister pass through the third connecting pipe with second stills intercommunication, the demister pass through the second connecting pipe with the upper portion intercommunication of second stills, the upper end of second stills is equipped with the formation section of thick bamboo portion, is equipped with a plurality of defoaming baffles in the section of thick bamboo portion.

As the preferred mode of the utility model, the exit end of cooler is equipped with the calandria, is equipped with alcoholic strength caliber and gas vent in the calandria.

As the utility model discloses an optimal mode still includes receipts winebowl, is equipped with the edulcoration groove in receiving the winebowl upper portion, the entrance point in edulcoration groove with the exit end intercommunication of calandria, the edulcoration inslot is equipped with the overflow pipe, and the lower extreme of overflow pipe extends to the bottom in edulcoration groove, and the upper end of overflow pipe forms the wine export, the wine export with receive the winebowl intercommunication.

As the preferable mode of the utility model, the bottom of the first distillation still and the bottom of the second distillation still are both provided with steam spray pipes for spraying hot steam.

Adopt the technical scheme of the utility model afterwards, the wine gas that comes out from first stills gets into in the second stills, get into wine gas conveyer pipe along with the wine gas in the second stills, wine gas conveyer pipe gets into the wine with the heat exchange of pre-heater, promote the temperature of wine with the dregs, later wine gas rethread cooler cools off and forms the beverage, because wine gas cools down through the pre-heater earlier, can reduce the work energy consumption of cooler, utilize the heat of wine gas to heat wine with the dregs simultaneously, wine with the dregs pass through the unloading pipe and get into the second stills, can reduce the energy consumption of second stills, through twice distillation, can promote alcohol concentration in the beverage. Preferably, the first distillation kettle and the second distillation kettle are communicated through a material pump, and the mash distilled in the second distillation kettle can be pumped into the first distillation kettle for further distillation, so that the distillation is more sufficient. The utility model discloses can distill out the high white spirit more than 50 degrees in succession, do not have low alcohol feints, energy-conservation more than 40%, practice thrift the cooling water more than 30%, be fit for liquid state fermentation's rice wine distillation and fruit wine distillation brandy.

Drawings

Fig. 1 is a schematic structural diagram of the present invention.

In the figure:

first distillation still 10 second distillation still 20

Defoaming partition 21 steam nozzle 22

Preheater 30 beer inlet 31

Cooler 40 wine discharge tube 50

Air outlet 51 alcoholic strength measurer 52

Wine collecting tank 60 impurity removing tank 70

Wine air delivery pipe 80 of overflow pipe 71

First condenser 81 second condenser 82

First condensing passage 83 and second condensing passage 84

Cooling coil 85 adapter tube 86

Demister 87 first connecting pipe 91

Second connection pipe 92 and third connection pipe 93

Blanking tube 94 first feed tube 101

Second feed pipe 102 discharge pipe 103

First control valve 104 second control valve 105

Third control valve 106 discharge valve 107

Material pump 108

Detailed Description

In order to further explain the technical solution of the present invention, the following embodiments are described in detail.

Referring to fig. 1, a liquid distiller for highly white spirit comprises a first distillation still 10, a second distillation still 20, a preheater 30 and a cooler 40, wherein an air outlet end of the first distillation still 10 is connected with an air inlet end of the second distillation still 20 through a first connecting pipe 91, a wine gas conveying pipe 80 is arranged in the preheater 30, and one end (specifically, the lower end) of the wine gas conveying pipe 80 penetrates through the preheater 30 and is communicated with the cooler 40, in the embodiment, is communicated with the cooler 40 through a connecting pipe 86. The other end of the wine gas conveying pipe 80 is communicated with the gas outlet end of the second distillation still 20, and the wine gas coming out of the second distillation still 20 enters the cooler through the wine gas conveying pipe 80. The preheater 30 is communicated with the second distillation kettle 20 through a discharge pipe 94, a mash charging port 31 is arranged in the preheater 30, the mash is arranged in the preheater 30 through the mash charging port 31, and the preheater 30 is in a tank shape. As the preferred mode of the utility model, the bottom of the first still 10 and the bottom of the second still 20 are all equipped with the steam spray pipe 22 that is used for spraying hot steam, and steam spray pipe 22 and hot steam source intercommunication, the structure of steam spray pipe 22 adopts annular steam spray pipe 22 for the structure of current white spirit distiller.

As the preferred mode of the present invention, the distillation still further comprises a material pump 108, the discharge port of the material pump 108 is communicated with the first distillation still 10 (specifically, connected to the upper end of the first distillation still 10) through the first feeding pipe 101, and the feed port of the material pump 108 is communicated with the bottom of the second distillation still 20 through the second feeding pipe 102. As a preferred mode of the present invention, a first control valve 104 is disposed on the first feeding pipe 101, a second control valve 105 is disposed on the second feeding pipe 102, and the first feeding pipe 101 is further provided with a discharge valve 107. As an optimized mode of the present invention, the lower end of the first distillation still 10 is further provided with a material discharging pipe 103, the material discharging pipe 103 is provided with a third control valve 106, one end of the material discharging pipe 103 is communicated with the lower end of the first distillation still 10, and the other end is communicated with the feed inlet of the material pump 108. With the above configuration, when it is desired to transfer the moromi in the second still pot 20 to the first still pot 10, the third control valve 106 and the discharge valve 107 are closed, and the first control valve 104 and the second control valve 105 are opened. When it is desired to discharge the moromi from the first still pot 10, the first control valve 104 and the second control valve 105 are closed, the third control valve 106 and the discharge valve 107 are opened, and the moromi is discharged through the discharge pipe 103 and the discharge valve 107.

As a preferred embodiment of the present invention, a first condenser 81 is provided in the preheater 30, and the first condenser 81 has a first condensation passage 83 provided in the transportation path of the wine gas transportation pipe 80 and communicating with the wine gas transportation pipe 80. In a preferred embodiment of the present invention, a second condenser 82 is provided in the cooler 40, and the second condenser 82 has a second condensation passage 84 provided in the transportation path of the wine gas transportation pipe 80 and communicating with the wine gas transportation pipe 80.

In a preferred embodiment of the present invention, a cooling coil 85 is further disposed in the cooler 40, and the cooling coil 85 is connected to cooling water (e.g., well water).

As a preferred mode of the present invention, a demister 87 is disposed above the preheater 30, the demister 87 is used for isolating foam in the wine gas in the demister 87 to improve the purity of the wine gas, the wine gas conveying pipe 80 extends to the upper portion of the demister 87, the demister 87 is communicated with the second still 20 through a third connecting pipe 93, specifically, both ends of the third connecting pipe 93 are connected to the middle portion of the demister 87 and the upper end portion of the second still 20, the demister 87 is communicated with the upper portion of the second still 20 through a second connecting pipe 92, specifically, both ends of the second connecting pipe 92 are connected to the lower end of the demister 87 and the upper portion of the second still 20, respectively, and when the wine mash in the preheater 30 is transferred to the second still 20, the gas in the second still 20 is compensated to the preheater 30. The upper end of the second distillation still 20 is provided with a forming cylinder part, a plurality of defoaming clapboards 21 are arranged in the cylinder part, and a bent channel is formed by the defoaming clapboards 21 to reduce the foam entering the wine gas conveying pipe 80.

As a preferred embodiment of the present invention, the outlet end of the cooler 40 is provided with a wine discharge pipe 50, an alcohol content measuring device 52 and an exhaust port 51 are provided in the wine discharge pipe, the exhaust port 51 can discharge low alcohol (methanol), and the alcohol content measuring device 52 can detect the alcohol concentration of the wine.

As the utility model discloses an optimal mode still includes receipts wine groove 60, is equipped with edulcoration groove 70 in receiving wine groove 60 upper portion, the entrance point of edulcoration groove 70 with the exit end intercommunication of calandria 50 is equipped with overflow pipe 71 in the edulcoration groove 70, and the lower extreme of overflow pipe 71 extends to the bottom of edulcoration groove 70, and the upper end of overflow pipe 71 forms the wine water export, the wine water export with receive wine groove 60 intercommunication, the wine water gets into from the wine water export and collects in receiving wine groove 60, can separate some fluid material fusel oil (float in the wine liquid) through overflow pipe 71 and keep off in edulcoration groove 70, regularly clear up again.

The utility model discloses at the during operation, first stills 10 and second stills 20 distill simultaneously, wine gas in the first stills 10 gets into second stills 20, accelerate the distillation of wine gas in the second stills 20, hot wine gas that comes out from second stills 20 passes through wine gas conveyer pipe 80 and gets into cooler 40, wine gas is when first condensing channel 83, carry out the heat exchange through the wine mash in first condenser 81 and the pre-heater 30, further cool off formation beverage through second condenser 82 and cooling coil 85, beverage gets into impurity removal groove 70 through wine discharge pipe 50, rethread overflow pipe 71 gets into and receives the beverage tank 60, the alcoholic strength can reach 60% (V/V). After a certain period of distillation, the alcohol content in the second distillation still 20 is reduced, the wine mash in the second distillation still 20 is pumped into the first distillation still 10 through the material pump 108, the preheated wine mash in the preheater 30 is discharged into the second distillation still 20 through the discharge pipe 94, distillation is carried out again, and after distillation, the wine mash in the first distillation still 10 is discharged through the material pump 108.

The product form of the present invention is not limited to the embodiment of the present invention, and any person can properly change or modify the product form of the present invention without departing from the scope of the present invention.

Claims

1. The utility model provides a high white spirit liquid distiller which characterized in that: including first stills, second stills, pre-heater and cooler, the end of giving vent to anger of first stills is connected through first connecting tube with the inlet end of second stills, is equipped with wine gas conveyer pipe in the pre-heater, and the one end of wine gas conveyer pipe is worn out the pre-heater and is communicate with the cooler, and the other end of wine gas conveyer pipe communicates with the end of giving vent to anger of second stills, and the pre-heater passes through unloading pipe and second stills intercommunication, is equipped with the wine liquid charging hole in the pre-heater.

2. The liquor distiller of claim 1, wherein: the material pump is further included, a discharge port of the material pump is communicated with the first distillation still through the first feeding pipe, and a feed port of the material pump is communicated with the bottom of the second distillation still through the second feeding pipe.

3. The liquor distiller of claim 2, wherein: the first feeding pipe is provided with a first control valve, the second feeding pipe is provided with a second control valve, and the first feeding pipe is further provided with a discharge valve.

4. The liquor distiller of claim 3, wherein: the lower extreme of first stills still is equipped with the row material pipe, arranges and is equipped with the third control valve on the material pipe, arrange the one end of material pipe with first stills's lower extreme intercommunication, the other end with the feed inlet intercommunication of material pump.

5. The liquor distiller of claim 1, wherein: the pre-heater is internally provided with a first condenser, and the first condenser is provided with a first condensing channel which is arranged on the conveying path of the wine gas conveying pipe and is communicated with the wine gas conveying pipe.

6. The liquor distiller of claim 5, wherein the liquor distiller comprises: and a second condenser is arranged in the cooler, and the second condenser is provided with a second condensation channel which is arranged on the conveying path of the wine air conveying pipe and is communicated with the wine air conveying pipe.

7. The liquid distiller for highly white spirit according to claim 6, wherein: and a cooling coil is also arranged in the cooler.

8. The liquor distiller of claim 1, wherein: the top of pre-heater is equipped with the demister, wine gas conveyer pipe extends to the upper portion of demister, the demister pass through the third connecting pipe with the second stills intercommunication, the demister pass through the second connecting pipe with the upper portion intercommunication of second stills, the upper end of second stills is equipped with and forms the section of thick bamboo portion, is equipped with a plurality of defoaming baffles in the section of thick bamboo portion.

9. The liquid distiller for highly white spirit according to claim 1, which is characterized in that: the exit end of cooler is equipped with the wine discharging pipe, is equipped with alcoholic strength caliber and gas vent in the wine discharging pipe, still including receiving the wineglass, is equipped with the edulcoration groove in receiving the wineglass upper portion, the entrance point in edulcoration groove with the exit end intercommunication of wine discharging pipe is equipped with the overflow pipe in the edulcoration groove, and the lower extreme of overflow pipe extends to the bottom in edulcoration groove, and the upper end of overflow pipe forms the wine export, and the wine export communicates with receipts wineglass.

10. The liquid distiller for highly distilled spirits of any one of claims 1 to 9, wherein: and the bottom of the first distillation kettle and the bottom of the second distillation kettle are both provided with steam spray pipes for spraying hot steam.