CN102860562B - Soft drink production device - Google Patents
Soft drink production device Download PDFInfo
- Publication number
- CN102860562B CN102860562B CN201110190757.8A CN201110190757A CN102860562B CN 102860562 B CN102860562 B CN 102860562B CN 201110190757 A CN201110190757 A CN 201110190757A CN 102860562 B CN102860562 B CN 102860562B
- Authority
- CN
- China
- Prior art keywords
- water
- valve
- pipe
- equiped
- bronchus
- 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
Links
Images
Landscapes
- Accessories For Mixers (AREA)
Abstract
The invention discloses a soft drink production device, which comprises an oxygen bottle, a gas collection tank, a mixing tank and a soft drink dilution mechanism. A water outlet of a plunger pump is connected with a water inlet of the mixing tank through a water delivery pipe. A gas outlet of the oxygen bottle is connected with a first gas inlet of the gas collection tank through a pipeline. The gas collection tank is provided with a plurality of gas branch pipes which are connected with the mixing tank and the water delivery pipe respectively. A soft drink outlet of the mixing tank is connected with a water inlet of a connecting pipe of the soft drink dilution mechanism through a soft drink delivery pipeline. The soft drink dilution mechanism comprises a soft drink flow divider and a water tank containing purified water. The soft drink flow divider is arranged in the water tank, and consists of a collecting pipe and a plurality of flow division pipes. The upper ends of the flow division pipes are connected with the collecting pipe respectively. A valve is arranged on each flow division pipe. The soft drink production device is simple in structure, high in production efficiency and energy-saving, and environmental pollution is reduced.
Description
Technical field
The present invention relates to a kind of beverage production settings, specifically a kind of water, carbon dioxide, oxygen or nitrogen powerful mixing are prepared the device of carbonated drink.
Background technology
Carbonated drink is that a kind of people like the beverage of drinking, and carbonated drink is exactly the aqueous solution of carbon dioxide, in current carbonated drink production process, in order to increase the solubility of carbon dioxide, except pressurizeing, also must carry out at low temperatures, therefore must be provided with refrigeration system.This not only increases equipment investment, has increased production cost, and power consumption is large, owing to there being the discharge of Fu Liang and ammonia, to environment.
In addition, in seawater, freshwater aquiculture or industrialization seedling raising process, needing oxygenating, avoid because anoxic causes the death of aquaculture thing, is mainly at present the way that increases dissolved oxygen in water with pump by pumping up water, and this way oxygenation effect is poor.
Summary of the invention
Object of the present invention, is to provide a kind of carbonated drink process units, can prepare fast the carbonated drink of oxygen enrichment or rich nitrogen, or carbonated carbonated drink, and simple in structure, and production efficiency is high.
The technical scheme adopting is:
A kind of carbonated drink process units, comprises plunger displacement pump or pressure water storage tank, has pressurized air source, plenum chamber; Blending tank and carbonated drink dilution mechanism;
The delivery port of plunger displacement pump or pressure water storage device is connected with the water inlet of blending tank by water-supply-pipe; The water inlet of plunger displacement pump or pressure water storage tank is connected with source of clean water by pipeline;
To have pressurized air source be oil-free air compressor, the oxygen cylinder of oxygen is housed or the nitrogen cylinder of nitrogen is housed; There is the gas outlet of pressurized air source to be connected with the first air inlet of plenum chamber by air delivering pipeline; On plenum chamber, be connected with the first bronchus, the second bronchus, the 3rd bronchus, the 4th bronchus and the 5th bronchus; The first bronchial other end is connected with the first air inlet of blending tank, is equiped with successively the first valve and the first check valve on the first bronchus, and the first check valve only allows the gas flow blending tank in plenum chamber while unlatching; The second bronchial other end is connected with the gas outlet of blending tank, on the second bronchus, be equiped with successively the second valve and the second check valve, the second check valve only allows the gas flow plenum chamber in blending tank while unlatching, the carbonated drink outlet of blending tank is connected with the water inlet of the header of carbonated drink dilution mechanism by carbonated drink transfer pipeline; Carbonated drink dilution mechanism comprises soda flow divider and the pond that pure water is housed, and soda flow divider is installed in pond, and is deep in pure water;
Described soda flow divider is made up of header and multiple isocon, and the upper end of multiple isocons is connected with header respectively, on each isocon, is equiped with valve.
The 3rd bronchus, the 4th bronchus and the 5th bronchial other end are connected with E, F, G place on water-supply-pipe respectively, on water-supply-pipe, on the first water-supply-pipe section between E point and F point, be equiped with the first centrifugal water pump or the first multi-stage centrifugal pump, on water-supply-pipe, on the second water-supply-pipe section between F point and G point, be equiped with the second centrifugal water pump or the second multi-stage centrifugal pump.
On hydraulic pipeline, can install multiple centrifugal water pumps or multi-stage water pump, the quantity of installing needs to determine according to the actual production of producing carbonated drink.
On hydraulic pipeline, in the 3rd line segments between delivery port and the E point of plunger displacement pump, be equiped with successively first flow meter, the 3rd check valve, the 3rd valve and the first control valve; On water-supply-pipe, on the 4th water-supply-pipe section between G point and the water inlet of blending tank, be equiped with successively the 4th valve, flow-through orifice, the 5th valve, the second flowmeter, the 6th valve and the second control valve.
On the 3rd bronchus, be equiped with respectively the 7th valve and the 4th check valve, on the 4th bronchus, be equiped with respectively the 8th valve and the 5th check valve, on the 5th bronchus, be equiped with respectively the 9th valve and the 6th check valve; When the 4th check valve, the 5th check valve and the 6th check valve are opened, only allow oxygen, nitrogen or flow of carbon dioxide gas to enter water-supply-pipe.
On appendix, be equiped with respectively Pressure gauge and pressure reducer, pressure reducer can guarantee that the gas pressure in input set gas tank reaches setting value.
On plenum chamber, be respectively equipped with the first Pressure gauge and the first safety valve, be connected with the first blow-off pipe on the lower surface of plenum chamber, be equiped with the tenth valve on the first blow-off pipe, the tenth valve is blowoff valve, and the other end of blow-off pipe inserts in the dirty pond of collection.
On the upper end cover of blending tank, be equiped with respectively the second Pressure gauge and the second safety valve, be connected with the second blow-off pipe on the diapire of blending tank, the other end of the second blow-off pipe is connected with the pollution discharge pond of peripheral hardware, is equiped with the 11 valve on the second blow-off pipe.
On carbonated drink transfer pipeline, be equiped with liquid medium pressure reducer, the 3rd flowmeter and valve.
Described liquid medium pressure reducer is that the silica gel lining arranging on the inwall of the metal tubes being converted into by dish and the metal tubes being converted at dish forms.
Operation principle of the present invention:
What produced by oil-free air compressor purifies air, or oxygen in oxygen cylinder, nitrogen in nitrogen cylinder injects plenum chamber 3, reach the setting pressure of need of production, Open valve 27, 30, 32, 34, open centrifugal pump or centrifugal multistage pump multiple centrifugal pump group 21, in the constant pressure water suction pump from plunger displacement pump or pressure water storage tank 1 or pump group 21, 8 enter blending tank 4 by the road, adjust flow control valve 28, 35 reach setting flow, Open valve 36, by gas suction pump or pump group 21, enter gas in pump and water carries out more refinement and mixes at many levels and generate high degree of mixing carbonated drink and 7 enter blending tank 4 by the road under water pump vane High Rotation Speed and pressure condition. Open valve 16,18, adjust pressure and the control valve 28,35 of pressure reducer 43, make system enter poised state and reach best air water mixed effect.
Input purify air or oxygen mix after pressure carbonated drink, enter soda flow divider 21 by pressure reducer 5 by pipeline 48, so as required to produce high degree of mixing carbonated drink dilute.
The mixed pressure carbonated drink of input nitrogen is controlled and is directly entered bulking system and corresponding production system by valve 53.
Carbonated drink process units range of application of the present invention comprises:
1, input purifies air or oxygen is applicable to oxygenation and the emergency rescue that seawater, freshwater fish aquaculture and industrialization are grown seedlings under anaerobic condition.
2, input nitrogen is applicable to food industry production, the super saturated steam water of nitrogen and pure water powerful mixing, the alternative blowing agent of dough, swelling agent that the wheaten food mixer of input sealing is produced.
The present invention is simple in structure, and production efficiency is high, saves the energy, makes new generation of green food, reduces disposal of pollutants.
Accompanying drawing explanation
Fig. 1 is a kind of example structure schematic diagram of the present invention.
Fig. 2 is pressure water storage tank structural representation, is known device.
The specific embodiment
Embodiment mono-
A kind of carbonated drink process units, comprises plunger displacement pump 1, has pressurized air source 2, plenum chamber 3, blending tank 4 and carbonated drink dilution mechanism;
The delivery port of plunger displacement pump 1 is connected with the water inlet of blending tank 4 by water-supply-pipe 7; The water inlet of plunger displacement pump 1 is connected with source of clean water by pipeline;
There is pressurized air source 2 for the oxygen cylinder of oxygen is housed; There is the gas outlet of pressurized air source 2 to be connected with the first air inlet 9 of plenum chamber 3 by air delivering pipeline 8; On plenum chamber 3, be connected with the first bronchus 10, the second bronchus 11, the 3rd bronchus 12, the 4th bronchus 13 and the 5th bronchus 14; The other end of the first bronchus 10 is connected with the first air inlet 55 of blending tank 4, is equiped with successively and when the first valve 16 and the first check valve 17, the first check valves 17 are opened, only allows the gas flow blending tank 4 in plenum chamber 3 on the first bronchus 10; The other end of the second tracheae is connected with the gas outlet of blending tank 4, on the second bronchus 11, be equiped with successively the second valve 18 and the second check valve 19, the second check valve only allows the gas flow plenum chamber 3 in blending tank 4 while unlatching, the carbonated drink outlet of blending tank 4 is connected with the water inlet of the header 58 of carbonated drink dilution mechanism by carbonated drink transfer pipeline 48; Carbonated drink dilution mechanism comprises soda flow divider 57 and the pond 61 that pure water is housed, and soda flow divider 57 is installed in pond 61, and is deep in pure water;
Described soda flow divider 57 is made up of header 58 and multiple isocon 59, and the upper end of multiple isocons 59 is connected with header 58 respectively, on each isocon 59, is equiped with valve 60.
The other end of the 3rd bronchus 12, the 4th bronchus 13 and the 5th bronchus 14 is connected with E, F, G place on water-supply-pipe 7 respectively, on water-supply-pipe 7, on the first water-supply-pipe section 20 between E point and F point, be equiped with the first centrifugal water pump 21, on water-supply-pipe 7, on the second water-supply-pipe section 22 between F point and G point, be equiped with the second centrifugal water pump 23.
On water-supply-pipe 7, on the 3rd water-supply-pipe section 24 between delivery port and the E point of plunger displacement pump 1, be equiped with successively first flow meter 25, the 3rd check valve 26, the 3rd valve 27 and the first control valve 28; On water-supply-pipe 7, on the 4th water-supply-pipe section 29 between G point and the water inlet 56 of blending tank 4, be equiped with successively the 4th valve 30, flow-through orifice 31, the 5th valve 32, the second flowmeter 33, the 6th valve 34 and the second control valve 35.
On the 3rd bronchus 12, be equiped with respectively the 7th valve 36 and the 4th check valve 37, on the 4th bronchus 13, be equiped with respectively the 8th valve 38 and the 5th check valve 39, on the 5th bronchus 14, be equiped with respectively the 9th valve 40 and the 6th check valve 41; When the 4th check valve 37, the 5th check valve 39 and the 6th check valve 41 are opened, only allow oxygen, nitrogen or flow of carbon dioxide gas to enter water-supply-pipe 7.
On appendix 8, be equiped with respectively Pressure gauge 42 and pressure reducer 43, pressure reducer 43 can guarantee that the gas pressure in input set gas tank 3 reaches setting value.
On plenum chamber 3, be respectively equipped with the first Pressure gauge 44 and the first safety valve 45, on the lower surface of plenum chamber 3, be connected with the first blow-off pipe 15, on the first blow-off pipe 15, being equiped with the tenth valve 46, the ten valves 46 is blowoff valve, and the other end of blow-off pipe 15 inserts in the dirty pond 47 of collection.
On the upper end cover of blending tank 4, be equiped with respectively the second Pressure gauge 6 and the second safety valve 49, on the diapire of blending tank, be connected with the second blow-off pipe 50, second other end of blow-off pipe 50 and the pollution discharge pond of peripheral hardware 47 are connected, and on the second blow-off pipe 50, are equiped with the 11 valve 51.
On carbonated drink transfer pipeline 48, be equiped with liquid medium pressure reducer 5, the 3rd flowmeter 52 and valve 53.
Described liquid medium pressure reducer 5 is that the silica gel lining arranging on the inwall of the metal tubes 54 being converted into by dish and the metal tubes 54 being converted at dish forms.
Claims (2)
1. a carbonated drink process units, comprises plunger displacement pump, has pressurized air source, plenum chamber; Blending tank and carbonated drink dilution mechanism;
The delivery port of plunger displacement pump is connected with the water inlet of blending tank by water-supply-pipe; The water inlet of plunger displacement pump is connected with source of clean water by pipeline;
To have pressurized air source be oil-free air compressor, the oxygen cylinder of oxygen is housed or the nitrogen cylinder of nitrogen is housed; There is the gas outlet of pressurized air source to be connected with the first air inlet of plenum chamber by air delivering pipeline; On plenum chamber, be connected with the first bronchus, the second bronchus, the 3rd bronchus, the 4th bronchus and the 5th bronchus; The first bronchial other end is connected with the first air inlet of blending tank, is equiped with successively the first valve and the first check valve on the first bronchus, and the first check valve only allows the gas flow blending tank in plenum chamber while unlatching; The second bronchial other end is connected with the gas outlet of blending tank, on the second bronchus, be equiped with successively the second valve and the second check valve, the second check valve only allows the gas flow plenum chamber in blending tank while unlatching, the carbonated drink outlet of blending tank is connected with the water inlet of the header of carbonated drink dilution mechanism by carbonated drink transfer pipeline; Carbonated drink dilution mechanism comprises soda flow divider and the pond that pure water is housed, and soda flow divider is installed in pond, and is deep in pure water;
Described soda flow divider is made up of header and multiple isocon, and the upper end of multiple isocons is connected with header respectively, on each isocon, is equiped with valve;
The 3rd bronchus, the 4th bronchus and the 5th bronchial other end are connected with water-supply-pipe respectively; Tie point on the 3rd bronchus and water-supply-pipe is E point, tie point on the 4th bronchus and water-supply-pipe is F point, tie point on the 5th bronchus and water-supply-pipe is G point, on water-supply-pipe, on the first water-supply-pipe section between E point and F point, be equiped with the first centrifugal water pump or the first multi-stage centrifugal pump, on water-supply-pipe, on the second water-supply-pipe section between F point and G point, be equiped with the second centrifugal water pump or the second multi-stage centrifugal pump;
On hydraulic pipeline, install multiple centrifugal water pumps or multi-stage water pump, the quantity of installing needs to determine according to the actual production of producing carbonated drink;
On hydraulic pipeline, in the 3rd line segments between delivery port and the E point of plunger displacement pump, be equiped with successively first flow meter, the 3rd check valve, the 3rd valve and the first control valve; On water-supply-pipe, on the 4th water-supply-pipe section between G point and the water inlet of blending tank, be equiped with successively the 4th valve, flow-through orifice, the 5th valve, the second flowmeter, the 6th valve and the second control valve;
On the 3rd bronchus, be equiped with respectively the 7th valve and the 4th check valve, on the 4th bronchus, be equiped with respectively the 8th valve and the 5th check valve, on the 5th bronchus, be equiped with respectively the 9th valve and the 6th check valve; When the 4th check valve, the 5th check valve and the 6th check valve are opened, only allow oxygen, nitrogen or flow of carbon dioxide gas to enter water-supply-pipe, it is characterized in that:
On appendix, be equiped with respectively Pressure gauge and pressure reducer, pressure reducer can guarantee that the gas pressure in input set gas tank reaches setting value;
On plenum chamber, be respectively equipped with the first Pressure gauge and the first safety valve, be connected with the first blow-off pipe on the lower surface of plenum chamber, be equiped with the tenth valve on the first blow-off pipe, the tenth valve is blowoff valve, and the other end of blow-off pipe inserts in the dirty pond of collection;
On the upper end cover of blending tank, be equiped with respectively the second Pressure gauge and the second safety valve, be connected with the second blow-off pipe on the diapire of blending tank, the other end of the second blow-off pipe is connected with the pollution discharge pond of peripheral hardware, is equiped with the 11 valve on the second blow-off pipe;
Described to have pressurized air source be oil-free air compressor, the oxygen cylinder of oxygen is housed or the nitrogen cylinder of nitrogen is housed;
The carbonated drink outlet of described blending tank is connected with the water inlet of the header of carbonated drink dilution mechanism by carbonated drink transfer pipeline; Carbonated drink dilution mechanism comprises soda flow divider and the pond that pure water is housed, and soda flow divider is installed in pond, and is deep in pure water;
Described soda flow divider is made up of header and multiple isocon, and the upper end of multiple isocons is connected with header respectively, on each isocon, is equiped with valve.
2. a kind of carbonated drink process units according to claim 1, it is characterized in that being equiped with liquid medium pressure reducer, the 3rd flowmeter and valve on carbonated drink transfer pipeline, described liquid medium pressure reducer is that the silica gel lining arranging on the inwall of the metal tubes being converted into by dish and the metal tubes being converted at dish forms.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110190757.8A CN102860562B (en) | 2011-07-08 | 2011-07-08 | Soft drink production device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110190757.8A CN102860562B (en) | 2011-07-08 | 2011-07-08 | Soft drink production device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102860562A CN102860562A (en) | 2013-01-09 |
| CN102860562B true CN102860562B (en) | 2014-05-14 |
Family
ID=47439912
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110190757.8A Expired - Fee Related CN102860562B (en) | 2011-07-08 | 2011-07-08 | Soft drink production device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102860562B (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10017373B2 (en) * | 2016-04-15 | 2018-07-10 | Automatic Bar Controls, Inc. | Nitrogen generator and uses thereof |
| CN110236391A (en) * | 2018-03-07 | 2019-09-17 | 佛山市顺德区美的饮水机制造有限公司 | Water dispenser and its soda water concentration control method and soda water concentration control apparatus |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2093578U (en) * | 1991-06-17 | 1992-01-22 | 韩鸿庆 | Small soda water making machine |
| DE19801695C1 (en) * | 1997-04-21 | 1999-05-27 | Tuchenhagen Gmbh | Process for starting up a liquid dosing system with in-line properties, especially in the production of soft drinks from water, syrup and carbon dioxide |
| CN201005502Y (en) * | 2006-11-14 | 2008-01-16 | 王冬雷 | Multifunctional beverage machine |
| CN201320088Y (en) * | 2008-12-01 | 2009-10-07 | 余建丰 | Steam-water separator and water dispenser |
| CN201388484Y (en) * | 2009-02-20 | 2010-01-27 | 黎永雄 | Domestic ice cream maker capable of preparing carbonated drinks |
-
2011
- 2011-07-08 CN CN201110190757.8A patent/CN102860562B/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| CN102860562A (en) | 2013-01-09 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204824868U (en) | Anaerobic jar marsh gas agitating unit | |
| CN204848855U (en) | Fermentation cylinder with multistage distribution of multilayer stirring | |
| CN101343108A (en) | Method for coupling treatment of sewage water of waterpower cavitation and ozone | |
| CN104211198A (en) | Aquaculture oxygen charging system | |
| CN102860562B (en) | Soft drink production device | |
| CN211746311U (en) | Fishpond oxygenation system based on static mixing | |
| CN203715367U (en) | Water distribution device of integral ozone-aeration biofilter | |
| CN103626281B (en) | Integrated ozone and biological aerated filter water distributing and air distributing device | |
| CN203803398U (en) | Micro gas-liquid mixing pump | |
| CN204569680U (en) | A kind of waste disposal plant | |
| CN208362323U (en) | A kind of pure oxygen fermentation system | |
| CN103493776A (en) | Gas exchange device for water circulating aquaculture | |
| CN202566172U (en) | Device used for increasing dissolved oxygen content in instant tea | |
| CN103897760A (en) | Marsh gas purification system | |
| CN203904058U (en) | Deep well aeration device | |
| CN201283235Y (en) | Modular high-efficient foam destroyer without power consumption | |
| CN203715368U (en) | Tubular aeration system | |
| CN201720060U (en) | Ion exchange resin regeneration liquid preparation device | |
| CN206051547U (en) | A kind of intelligent ozone generator | |
| CN212334720U (en) | Gravity type negative pressure self-oxygenating pipeline device | |
| CN202465363U (en) | Low pressure oxygenation jet apparatus | |
| CN201221818Y (en) | Sterilization air conditioning apparatus of central air conditioner pipeline | |
| CN213834531U (en) | Novel methanol cracking hydrogen production device | |
| CN201062257Y (en) | Agitating means used in white spirit blending process | |
| CN2913343Y (en) | Energy-saving second level reverse osmosis apparatus |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140514 Termination date: 20150708 |
|
| EXPY | Termination of patent right or utility model |