CN104664542A - Secondary degassing device of mixer - Google Patents
Secondary degassing device of mixer Download PDFInfo
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- 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
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- mixer
- water
- degassing tank
- degassing
- deoxidation
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- Degasification And Air Bubble Elimination (AREA)
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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 |
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CN201410820840.2A CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
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CN201410820840.2A CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
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CN104664542A true CN104664542A (en) | 2015-06-03 |
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CN201410820840.2A Pending CN104664542A (en) | 2014-12-26 | 2014-12-26 | Secondary degassing device of mixer |
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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)
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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 | Deaerator And Method For Deaeration |
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2014
- 2014-12-26 CN CN201410820840.2A patent/CN104664542A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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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 | Deaerator And Method For Deaeration |
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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Application publication date: 20150603 |