CN209685737U - Ester enrichment facility in white wine - Google Patents
Ester enrichment facility in white wine Download PDFInfo
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- CN209685737U CN209685737U CN201920316163.9U CN201920316163U CN209685737U CN 209685737 U CN209685737 U CN 209685737U CN 201920316163 U CN201920316163 U CN 201920316163U CN 209685737 U CN209685737 U CN 209685737U
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- nitrogen
- white wine
- enrichment facility
- liquid
- cooling cylinder
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Abstract
The utility model relates to Liquor Analysis testing equipment fields, especially a kind of quick and while obtaining the white wine of highly enriched degree of efficiency, greatly save Ester enrichment facility in the white wine of the energy, including distillation still, cooling cylinder and liquid storing barrel, by being connected at the top of exhaust pipe and cooling cylinder at the top of the distillation still, cooling cylinder bottom is connected to liquid storing barrel, wherein the bottom in the distillation still is provided with nitrogen blowing apparatus and heating device.The utility model has carried out creative optimization for white wine concentration distillation process, both improves distillation efficiency, reduce extra moisture evaporation, and quickly and efficiently rate obtains the white wine of highly enriched degree, and reduces cost of labor, save electricity.Wine liquid is stirred from wine liquid bottom by nitrogen, acceleration of alcohol evaporation is exchanged heat by white wine steam and low temperature nitrogen, saves the use of cooling water, reduced the electric energy consumed required for heated nitrogen, the energy is greatly saved.The utility model is particularly suitable among white wine concentration distillation.
Description
Technical field
The utility model relates to Liquor Analysis testing equipment field, Ester enrichment facility in especially a kind of white wine.
Background technique
Currently, Liquor-making Technology with Uncooked mostly uses greatly liquid state fermentation, liquid distillate to take wine technique.Existing wine brewing distilling apparatus
In, the condenser wall area of condenser unit volume is smaller, and the heating surface area of steaming bucket unit volume is also smaller, distills existing when taking wine
Wine brewing distilling apparatus there is energy consumptions that shortcoming high, that production efficiency is low is required to during white liquor distilling by cooling down
Water carries out cooling so that white wine is obtained, by the used cooling water sheet of white liquor distilling in a manner of heat exchange to the wine vapour of white wine
Body temperature has just been increased to 50-65 DEG C by room temperature, later, has just used this and cold containing 50-65 DEG C of temperature
But water is discarded and is discharged, and is carried out continuously in this way, the distillation process of white wine is without stop, had been used and had been contained 50-65
The cooling water of DEG C temperature is just carried out continuously discarded and discharges, to cause the significant wastage of water resource.
Utility model content
It is quick and efficiency the technical problem to be solved by the utility model is to provide one kind to obtain the white wine of highly enriched degree
While, greatly save Ester enrichment facility in the white wine of the energy.
The technical scheme adopted by the utility model to solve the technical problem is as follows: Ester enrichment facility in white wine, packet
Include distillation still, cooling cylinder and liquid storing barrel, by being connected at the top of exhaust pipe and cooling cylinder at the top of the distillation still, cooling cylinder bottom and
Liquid storing barrel connection, wherein the bottom in the distillation still is provided with nitrogen blowing apparatus and heating device.
Further, the nitrogen blowing apparatus includes the nitrogen blow tube construction for the bottom being set in distillation still.
Further, the nitrogen blow tube construction is by air distribution disk and is uniformly distributed in the gas-distributing pipe structure on air distribution disk periphery
At.
Further, the nitrogen blowing apparatus includes nitrogen feed system, the nitrogen feed system by liquid nitrogen container and with
The spiral nitrogen tube of liquid nitrogen container connection is constituted, wherein the spiral nitrogen tube is set in cooling cylinder, nitrogen blow tube construction and spiral
Nitrogen tube connection.
Further, being provided between the liquid nitrogen container and spiral nitrogen tube from pressurized exhaust gas valve.
Further, nitrogen heating system is provided between nitrogen blow tube construction and spiral nitrogen tube, the nitrogen heating
System is made of the temperature-sensing pipe that connect with nitrogen blow tube construction, nitrogen heater box, the heating net being set in nitrogen heater box.
Further, including the power regulator for being provided with controller, the heating device is connect with power regulator.
Further, remote level indicator is provided in the liquid storing barrel, the remote level indicator and power supply pressure stabilizing
Device connection.
Further, being provided with exhaust outlet at the top of the liquid storing barrel.
Further, the outer wall of cooling cylinder is provided with heat sink.
The beneficial effects of the utility model are: the utility model has carried out the excellent of creativeness for white wine concentration distillation process
Change, both improve distillation efficiency, reduce extra moisture evaporation, quickly and efficiently rate obtains the white wine of highly enriched degree, again
Reduce cost of labor, save electricity.Wine liquid is stirred from wine liquid bottom by nitrogen, acceleration of alcohol evaporation is steamed by white wine
Vapour and low temperature nitrogen heat exchange, had not only saved the use of cooling water, but also reduce the electric energy consumed required for heated nitrogen, had saved significantly
The about energy.The utility model is particularly suitable among white wine concentration distillation.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Fig. 2 is the structural schematic diagram of the heating device of the utility model.
Fig. 3 is the structural schematic diagram of the nitrogen blowing apparatus of the utility model.
In the figure, it is marked as distillation still 1, heating device 2, nitrogen blowing apparatus 3, exhaust pipe 4, cooling cylinder 5, spiral nitrogen tube 6, storage
Liquid bucket 7, remote level indicator 8, from pressurized exhaust gas valve 9, liquid nitrogen container 10, nitrogen heater box 11, temperature-sensing pipe 12, heating net 13, electricity
Source voltage-stablizer 14, controller 15, side wall observation panel 16.
Specific embodiment
Ester enrichment facility in white wine as shown in Figure 1, Figure 2, Figure 3 shows, including distillation still 1, cooling cylinder 5 and liquid storing barrel
7, by being connected at the top of exhaust pipe 4 and cooling cylinder 5 at the top of the distillation still 1,5 bottom of cooling cylinder is connected to liquid storing barrel 7, wherein
Bottom in the distillation still 1 is provided with nitrogen blowing apparatus 3 and heating device 2.
In actual use, white wine to be concentrated is placed in distillation still first, then passes through nitrogen blowing apparatus and heating
Device carries out heating to white wine and nitrogen is blown；Then, the white wine of evaporation is entered in cooling cylinder by exhaust pipe, wherein alcohol is logical
Supercooling cylinder and condense and converge in liquid storing barrel；Finally, using triple quadrupole bar gas chromatograph-mass spectrometer to obtaining in liquid storing barrel
Concentration white wine is detected, and detects the content of Pfansteihl methyl esters and 2 methyl valeric acid ethyl ester in white wine.The utility model
In structure design, the effect that nitrogen blows and heats sufficiently is enhanced, effectively saves the use of cooling water, and reduces heated nitrogen institute
The electric energy of consumption.The white wine of the concentration obtained in liquid storing barrel can carry out Pfansteihl by triple quadrupole bar gas chromatograph-mass spectrometer
The detection of the content of methyl esters and 2 methyl valeric acid ethyl ester.The said structure design of the utility model finally both improves distillation effect
Rate, and reduce extra moisture evaporation, quickly and efficiently rate obtains the white wine of highly enriched degree, reduces cost of labor, saves
About electricity consumption stirs wine liquid from wine liquid bottom by nitrogen, and acceleration of alcohol evaporation is exchanged heat by white wine steam and low temperature nitrogen,
Not only the use of cooling water had been saved, but also has reduced the electric energy consumed required for heated nitrogen, the energy is greatly saved.
As the scheme of optimization, the preferably described nitrogen blowing apparatus 3 includes the nitrogen blowpipe knot for the bottom being set in distillation still 1
Structure.As shown in Figure 1, the nitrogen blow tube construction can choose by air distribution disk and be uniformly distributed in the gas-distributing pipe structure on air distribution disk periphery
At.Such structure design can uniformly, efficiently realize the input of nitrogen, thus strengthen white wine concentration process, meanwhile, also lead to
Raising nitrogen service efficiency is crossed to reduce electric energy consumed by heated nitrogen.
For nitrogen blowing apparatus 3, can choose following scheme: the nitrogen blowing apparatus 3 includes nitrogen feed system, the nitrogen
Gas feed system is made of liquid nitrogen container 10 and the spiral nitrogen tube 6 being connected to liquid nitrogen container 10, wherein the spiral nitrogen tube 6 is arranged
In in cooling cylinder 5, nitrogen blow tube construction is connected to spiral nitrogen tube 6.As shown in Figure 1, spiral nitrogen tube 6 is set in cooling cylinder 5,
It can realize to the preheating of nitrogen while condensing white wine steam, energy consumption not only can be effectively reduced, meanwhile, it also allows white
The condensation effect of wine is very ideal.Generally, in order to guarantee the stability of nitrogen supply (NS), the preferably described liquid nitrogen container 10 and spiral nitrogen
It is arranged between pipe 6 from pressurized exhaust gas valve 9.
In addition, in order to realize the stable dynamic control of nitrogen, so that the dynamic stability of input nitrogen temperature is realized automatically,
It can choose such scheme: being provided with nitrogen heating system, the nitrogen heating between nitrogen blow tube construction and spiral nitrogen tube 6
System by connect with nitrogen blow tube construction temperature-sensing pipe 12, nitrogen heater box 11, the heating net 13 being set in nitrogen heater box 11
It constitutes.In actual use, the nitrogen after 13 pairs of heating net preheatings is further heated, and the temperature of heating is to set
Temperature, the nitrogen temperature after wherein temperature-sensing pipe 12 can be heated with real-time detection, and whether will need heat etc. information feedback arrive
At heating net 13, to realize the Dynamic Stability Control of temperature.
For the controlled effect of power supply to heating device 2, preferably following scheme: the electricity including being provided with controller 15
Source voltage-stablizer 14, the heating device 2 are connect with power regulator 14.Herein on basis, in order to realize that heating device 2 heats
Linkage between power and concentration white wine amount, is arranged remote level indicator 8, the electric contact liquid preferably in the liquid storing barrel 7
Position meter 8 is connect with power regulator 14.White wine amount is concentrated in 8 real-time detection of remote level indicator, stores up when remote level indicator 8 incudes
When liquid in liquid bucket 7 reaches the one third of capacity, then the power supply output of heating device 2 is disconnected, so that remaining white wine is molten
Liquid slowly evaporates alcohol by high temperature nitrogen, which is distilled out by the induction of remote level indicator 8 in liquid storing barrel 7
White wine capacity, do not influenced by the wine liquid seethed in evaporation repeatedly, and change the distillation mode of white wine by controller, both improved
Distillation efficiency has been reduced extra moisture evaporation.
In order to allow the nitrogen converged in liquid storing barrel 7 to have the channel of discharge, exhaust is provided at the top of the preferably described liquid storing barrel 7
Mouthful.In addition, the outer wall that can choose in cooling cylinder 5 is provided with heat sink in order to strengthen the heat dissipation effect of cooling cylinder 5.
The utility model has carried out creative optimization for white wine concentration distillation process, both improves distillation efficiency, subtracts
Extra moisture evaporation is lacked, quickly and efficiently rate obtains the white wine of highly enriched degree, and reduces cost of labor, using electricity wisely
Amount.Wine liquid is stirred from wine liquid bottom by nitrogen, acceleration of alcohol evaporation is exchanged heat by white wine steam and low temperature nitrogen, both saved
The use of cooling water, and reduce the electric energy consumed required for heated nitrogen, it is greatly saved the energy, market promotion prospect ten
Divide wide.
Claims (10)
1. Ester enrichment facility in white wine, it is characterised in that: including distillation still (1), cooling cylinder (5) and liquid storing barrel (7), institute
It states by being connected at the top of exhaust pipe (4) and cooling cylinder (5) at the top of distillation still (1), cooling cylinder (5) bottom is connected to liquid storing barrel (7),
Wherein, the bottom in the distillation still (1) is provided with nitrogen blowing apparatus (3) and heating device (2).
2. Ester enrichment facility in white wine as described in claim 1, it is characterised in that: the nitrogen blowing apparatus (3) includes
It is set to the nitrogen blow tube construction of the bottom in distillation still (1).
3. Ester enrichment facility in white wine as claimed in claim 2, it is characterised in that: the nitrogen blow tube construction is by dividing gas
Disk and the gas-distributing pipe for being uniformly distributed in air distribution disk periphery are constituted.
4. Ester enrichment facility in white wine as claimed in claim 2 or claim 3, it is characterised in that: nitrogen blowing apparatus (3) packet
Nitrogen feed system is included, the nitrogen feed system is by liquid nitrogen container (10) and the spiral nitrogen tube (6) being connected to liquid nitrogen container (10)
It constitutes, wherein the spiral nitrogen tube (6) is set in cooling cylinder (5), nitrogen blow tube construction is connected to spiral nitrogen tube (6).
5. Ester enrichment facility in white wine as claimed in claim 4, it is characterised in that: the liquid nitrogen container (10) and spiral
It is provided between nitrogen tube (6) from pressurized exhaust gas valve (9).
6. Ester enrichment facility in white wine as claimed in claim 4, it is characterised in that: nitrogen blow tube construction and spiral nitrogen
Nitrogen heating system is provided between pipe (6), and the nitrogen heating system is by the temperature-sensing pipe (12), the nitrogen that connect with nitrogen blow tube construction
Gas heater box (11), the heating net (13) being set in nitrogen heater box (11) are constituted.
7. Ester enrichment facility in white wine as claimed in claim 1,2 or 3, it is characterised in that: including being provided with control
The power regulator (14) of device (15), the heating device (2) connect with power regulator (14).
8. Ester enrichment facility in white wine as claimed in claim 7, it is characterised in that: setting in the liquid storing barrel (7)
Have remote level indicator (8), the remote level indicator (8) connect with power regulator (14).
9. Ester enrichment facility in white wine as claimed in claim 1,2 or 3, it is characterised in that: liquid storing barrel (7) top
Portion is provided with exhaust outlet.
10. Ester enrichment facility in white wine as claimed in claim 1,2 or 3, it is characterised in that: outside cooling cylinder (5)
Wall is provided with heat sink.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920316163.9U CN209685737U (en) | 2019-03-13 | 2019-03-13 | Ester enrichment facility in white wine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920316163.9U CN209685737U (en) | 2019-03-13 | 2019-03-13 | Ester enrichment facility in white wine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209685737U true CN209685737U (en) | 2019-11-26 |
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ID=68604616
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201920316163.9U Active CN209685737U (en) | 2019-03-13 | 2019-03-13 | Ester enrichment facility in white wine |
Country Status (1)
| Country | Link |
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| CN (1) | CN209685737U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109762712A (en) * | 2019-03-13 | 2019-05-17 | 四川剑南春（集团）有限责任公司 | Ester enrichment facility and liquor determination method in white wine |
-
2019
- 2019-03-13 CN CN201920316163.9U patent/CN209685737U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109762712A (en) * | 2019-03-13 | 2019-05-17 | 四川剑南春（集团）有限责任公司 | Ester enrichment facility and liquor determination method in white wine |
| CN109762712B (en) * | 2019-03-13 | 2024-05-24 | 四川剑南春（集团）有限责任公司 | Device for concentrating esters in white spirit and white spirit detection method |
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