CN104664542A - Secondary degassing device of mixer - Google Patents
Secondary degassing device of mixer Download PDFInfo
- Publication number
- CN104664542A CN104664542A CN201410820840.2A CN201410820840A CN104664542A CN 104664542 A CN104664542 A CN 104664542A CN 201410820840 A CN201410820840 A CN 201410820840A CN 104664542 A CN104664542 A CN 104664542A
- Authority
- CN
- China
- Prior art keywords
- mixer
- water
- degassing tank
- degassing
- deoxidation
- 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.)
- Pending
Links
- 238000007872 degassing Methods 0.000 title claims abstract description 39
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 60
- 239000007788 liquid Substances 0.000 claims abstract description 14
- 238000005507 spraying Methods 0.000 claims abstract description 8
- 238000000889 atomisation Methods 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 239000007789 gas Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 235000013361 beverage Nutrition 0.000 abstract description 3
- 238000003763 carbonization Methods 0.000 abstract description 2
- 238000000926 separation method Methods 0.000 abstract 2
- 235000014171 carbonated beverage Nutrition 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 108010041986 DNA Vaccines Proteins 0.000 description 1
- 229940021995 DNA vaccine Drugs 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention relates to the technical field of degassing production equipment of a beverage mixer and particularly relates to a secondary degassing device of a mixer. The device comprises a horizontal degassing tank, a water inlet valve, a secondary degassing water inlet valve, a vacuum pump, a separation plate, a nozzle, a secondary circulating water pump and a continuous working pump, wherein the inner part of the horizontal degassing tank is divided into two independent spraying regions; and the horizontal degassing tank is divided into the two independent spraying regions by the separation plate with the special shape, and the liquid level of the horizontal degassing tank is guaranteed by a liquid level meter and the control of the water inlet valve and the secondary degassing water inlet valve. According to the secondary degassing device of the mixer, the degassing effect of the large-yield mixer is improved; under the condition that the manufacturing cost of the equipment is considered and the appearance size of the equipment is not too large, a conventional oxygen removing manner (primary oxygen removal) has unsatisfactory oxygen removing rate when being used for the large-yield mixer so that the dissolving of gas in a carbonization process of a post procedure is influenced, the freshness of products is not easy to keep, and the quality of the products is influenced.
Description
Technical field
The present invention relates to the degassed production equipment technical field of a kind of beverage mixer, specifically, is a kind of mixer secondary degasser.
Background technology
Along with rapid economic development, fruit juice, carbonated beverage become people's common consumer product, and carbonated beverage is beverage family important branch.Gassiness type is now also varied, and modal is soda, and also increasing with the demand of the fast development large output mixer of economy.
Large output mixer is one of necessary equipment complying with the growth of carbonated beverage market, and degasser is mixer important component part, and degasser performance directly affects product quality and product is fresh-keeping.Current domestic production equipment has vacuum outgas, replace degassed two kinds, the most common is vertical tank vacuum outgas, this degassed surface area is little, degassing efficiency is low, and the secondary deoxidations with the bedroom tank in two independent sprinkling regions increase deoxidation area, extend deaeration time, adapt to the requirement of market to large output mixer performance.
Summary of the invention
The object of the invention is the deoxidation effect improving large output mixer, optimizes the degassed index of large output mixer, is achieved through the following technical solutions:
The invention provides a kind of mixer secondary degasser, comprise inside and be separated into two independent horizontal degassing tanks spraying region, water intaking valve, the degassed water intaking valve of secondary, vavuum pump, dividing plate, nozzle, secondary cycle water pump and water pump of working continuously, it is characterized in that: be arranged in frame, inside is separated into two independent described horizontal degassing tanks spraying region, described water intaking valve is connected with described horizontal degassing tank by pipeline with the degassed water intaking valve of described secondary, some described nozzles are arranged on inlet channel, described vavuum pump is connected with described horizontal degassing tank by pipeline, water after deoxidation is first pumped to degassing tank and carries out secondary deoxidation by described secondary cycle water pump again, described water pump of working continuously pumps the water after secondary deoxidation.
Described inside is that two independent sprinklings in the horizontal degassing tank in region install some described nozzles by baffle for separating, liquid level gauge detects liquid level and selects to open water intaking valve and the degassed water intaking valve of secondary, water after first deoxidation is again pumped to through secondary cycle water pump and describedly horizontally degassedly carries out secondary deoxidation, described vavuum pump ensures the vacuum required for described horizontal degassing tank, nozzle ejection liquid obtains high atomisation, fully let go in described horizontal degassing tank, there is large surface area, and extended deaeration time through described secondary cycle water pump and described nozzle; Gas soluble in water extracted continuously out by described vavuum pump.
The good effect that the present invention has is:
The present invention improves large output mixer degasifying effect, under consideration equipment making cost and the unlikely prerequisite making contour size of the unit(s) excessive, when conventional deoxidation mode (deoxidation) is on large output mixer, DNA vaccine is undesirable, affect gas in later process carbonisation to dissolve in, be unfavorable for that product is fresh-keeping, affect product quality.
Accompanying drawing explanation
Below in conjunction with the embodiment in accompanying drawing, the present invention is described in further detail, but do not form any limitation of the invention.
Fig. 1 is the P & ID structural representation of a kind of mixer secondary of embodiments of the invention degasser;
Fig. 2 is the structural representation of a kind of mixer secondary of embodiments of the invention degasser;
Fig. 3 is the deoxidation schematic diagram of a kind of mixer secondary of embodiments of the invention degasser.
Wherein, 1, horizontal degassing tank, 2, water intaking valve, 3, the degassed water intaking valve of secondary, 4, liquid level gauge, 5, vavuum pump, 6, secondary cycle water pump, 7, water pump of working continuously, 8, dividing plate, 9, nozzle.
Detailed description of the invention
In order to make the object of the invention, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the present invention is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the present invention, and be not used in restriction invention.
Fig. 1 is the P & ID structural representation of a kind of mixer secondary of embodiments of the invention degasser.
The present invention relates to a kind of mixer secondary degasser, comprise inside and be separated into two independent horizontal degassing tanks 1 spraying region, water intaking valve 2, the degassed water intaking valve 3 of secondary, liquid level gauge 4, vavuum pump 5, dividing plate 8, nozzle 9, secondary cycle water pump 6 and water pump 7 of working continuously, it is characterized in that: be arranged in frame, inside is separated into two independent horizontal degassing tanks 1 spraying region, water intaking valve 2 is connected with horizontal degassing tank 1 by pipeline with the degassed water intaking valve of secondary 3, some nozzles 9 are arranged on inlet channel, vavuum pump 5 is connected with horizontal degassing tank 1 by pipeline, water after deoxidation is first pumped to degassing tank and carries out secondary deoxidation by secondary cycle water pump 6 again, water pump 7 of working continuously pumps the water after secondary deoxidation.
The inner horizontal degassing tanks 1 being divided into two independent sprinkling regions by dividing plate 8, some nozzles 9 are wherein installed, the liquid level gauge 4 arranged detects liquid level and selects to open water intaking valve 2 and the degassed water intaking valve 3 of secondary, water after first deoxidation is again pumped to horizontal degassing tank 1 through secondary cycle water pump 6 and carries out secondary deoxidation, vavuum pump 5 ensures the desired vacuum of horizontal degassing tank 1, nozzle 9 sprays liquid and obtains high atomisation, fully let go in horizontal degassing tank 1, there is large surface area, and extended deaeration time through secondary cycle water pump 6 and nozzle 9; Vavuum pump 5 extracts gas soluble in water out continuously.
The technological process of mixer may be summarized to be two steps: carbonating before this, is then that the water of carbonating mixes with the medium that will mix.The treated water (abbreviation process water) drinking standard of eating that conforms with enters horizontal deoxidation tank 1 by the nozzle injection having the display glass of coarse strainer and piston control to be transported to the effect of hazing, meanwhile, the mode that the carbon dioxide in carbonation tank overhead is connected with pipeline through pressure-reducing valve, flow valve and piston control valve etc. enters horizontal deoxidation tank 1, can remove the oxygen in compounding substances through horizontal deoxidation tank 1 deoxidation process of twice well.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any amendments done within the spirit and principles in the present invention, equivalent replacement and improvement etc., all should be included within protection scope of the present invention.
Claims (2)
1. a mixer secondary degasser, comprise inside and be separated into two independent horizontal degassing tanks (1) spraying region, water intaking valve (2), the degassed water intaking valve of secondary (3), liquid level gauge (4), vavuum pump (5), dividing plate (8), nozzle (9), secondary cycle water pump (6) and water pump of working continuously (7), it is characterized in that: be arranged in frame, inside is separated into two independent described horizontal degassing tanks (1) spraying region, described water intaking valve (2) is connected with described horizontal degassing tank (1) by pipeline with the degassed water intaking valve of described secondary (3), described nozzle (9) is arranged on inlet channel, described vavuum pump (5) is connected with described horizontal degassing tank (1) by pipeline, water after deoxidation is first pumped to degassing tank and carries out secondary deoxidation by described secondary cycle water pump (6) again, described water pump of working continuously (7) pumps the water after secondary deoxidation.
2. a kind of mixer secondary degasser according to claim 1, it is characterized in that, described inside is divided into two independent sprinklings in the horizontal degassing tank (1) in region by dividing plate (8) and is provided with described nozzle (9), liquid level gauge (4) detects liquid level and selects to open water intaking valve (2) and the degassed water intaking valve of secondary (3), water after first deoxidation is again pumped to described horizontal degassing tank (1) through secondary cycle water pump (6) and carries out secondary deoxidation, described vavuum pump (5) ensures the vacuum required for described horizontal degassing tank (1), described nozzle (9) ejection liquid obtains high atomisation, fully let go in described horizontal degassing tank (1), there is large surface area, and extended deaeration time through described secondary cycle water pump (6) and described nozzle (9), described vavuum pump (5) extracts gas soluble in water out continuously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410820840.2A CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410820840.2A CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104664542A true CN104664542A (en) | 2015-06-03 |
Family
ID=53300547
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410820840.2A Pending CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104664542A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110393951A (en) * | 2018-04-24 | 2019-11-01 | 克朗斯股份公司 | The method and beverage treatment machine of the degasification technique of degassing system and execution liquid |
| CN116458590A (en) * | 2023-03-28 | 2023-07-21 | 爱罗科(青岛)实业有限公司 | Soft and refreshing process for soda water |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0673606A1 (en) * | 1994-03-23 | 1995-09-27 | Manfred Dr.-Ing. Mette | Process and device for producing still beverages containing fruit juice |
| CN200987353Y (en) * | 2006-08-31 | 2007-12-12 | 钱志财 | Beverage mixer |
| CN201491680U (en) * | 2009-07-07 | 2010-06-02 | 合肥中辰轻工机械有限公司 | Improved beverage mixer degasser |
| CN103892400A (en) * | 2012-12-29 | 2014-07-02 | 上海沃迪自动化装备股份有限公司 | Full-automatic juice degasser |
| CN104010709A (en) * | 2011-12-21 | 2014-08-27 | 利乐拉瓦尔集团及财务有限公司 | Degasser and method for degassing |
-
2014
- 2014-12-26 CN CN201410820840.2A patent/CN104664542A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0673606A1 (en) * | 1994-03-23 | 1995-09-27 | Manfred Dr.-Ing. Mette | Process and device for producing still beverages containing fruit juice |
| CN200987353Y (en) * | 2006-08-31 | 2007-12-12 | 钱志财 | Beverage mixer |
| CN201491680U (en) * | 2009-07-07 | 2010-06-02 | 合肥中辰轻工机械有限公司 | Improved beverage mixer degasser |
| CN104010709A (en) * | 2011-12-21 | 2014-08-27 | 利乐拉瓦尔集团及财务有限公司 | Degasser and method for degassing |
| CN103892400A (en) * | 2012-12-29 | 2014-07-02 | 上海沃迪自动化装备股份有限公司 | Full-automatic juice degasser |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110393951A (en) * | 2018-04-24 | 2019-11-01 | 克朗斯股份公司 | The method and beverage treatment machine of the degasification technique of degassing system and execution liquid |
| US11014023B2 (en) | 2018-04-24 | 2021-05-25 | Krones Ag | Degassing system and method of executing a degassing process of a liquid and beverage treatment machine |
| CN116458590A (en) * | 2023-03-28 | 2023-07-21 | 爱罗科(青岛)实业有限公司 | Soft and refreshing process for soda water |
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| C06 | Publication | ||
| PB01 | Publication | ||
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| WD01 | Invention patent application deemed withdrawn after publication | ||
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Application publication date: 20150603 |