CN202425565U - Degasser using steam for evacuation and as heating medium - Google Patents
Degasser using steam for evacuation and as heating medium Download PDFInfo
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- CN202425565U CN202425565U CN 201120573144 CN201120573144U CN202425565U CN 202425565 U CN202425565 U CN 202425565U CN 201120573144 CN201120573144 CN 201120573144 CN 201120573144 U CN201120573144 U CN 201120573144U CN 202425565 U CN202425565 U CN 202425565U
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Abstract
The utility model discloses a degasser using steam for evacuation and as a heating medium, belongs to the technical field of degassing in production processes of fruit juice, fruit pulp and the like, and aims to overcome the defect that a supporting system of an existing vacuum degasser is complex, requires high electricity consumption and the like. The degasser using steam for evacuation and as the heating medium comprises a tank, a feed inlet, a delivery pump, a delivery pipe, an adjusting valve, a spray pipe and a hot water box. A liquid heating pipe is mounted inside the hot water tank, an inlet of the liquid heating pipe is communicated with an outlet of the delivery pump through the delivery pipe, and an outlet of the liquid heating pipe is communicated with the spray pipe through the delivery pipe and the adjusting valve. A steam jet is mounted on the upper portion of the tank and is communicated with an inner cavity of the tank through a suction pipe and a suction adjusting valve. A steam inlet of the steam jet is connected with a steam supply pipe and a steam supply valve, a steam reuse pipe is mounted at a steam outlet of the steam jet, and an outlet of the steam reuse pipe extends into the hot water box in water. The degasser is applicable to manufacturers of fruit juice, fruit pulp or other drinks.
Description
Technical field
The utility model relates to the degassing technology in the production technology such as a kind of fruit juice pulp, particularly relates to a kind ofly vacuumizing and the degasser of double as heating heating agent with steam.
Background technology
In food processing enterprises, general will be the processing that outgases of the stoste material of fruit juice, pulp or beverage to final products all.This is because in the production process of stoste material; The gas that fruit itself is contained all can be mixed in the stoste material with extraneous gas of sneaking into; And the stoste material has the character of thickness, and gas is again to be scattered in the stoste material with superfine little individuality, so generally can not overflow voluntarily.There is gas in the stoste material; Will influence the quality of final products, for example: make product brown stain, the useful composition of oxidation and nutrient, can be attached to make on slurry plasmid particle float, when can and sterilization product bubble, corrosion that can exacerbate packet tinning inwall etc.At present; Food processing enterprises generally all adopt vacuum degassing machine to the processing that outgases of the stoste material of fruit juice, pulp or beverage, and this degasser belongs to the vacuum spraying formula, and the effect of the degassing is reasonable; But; The corollary system that needs more complicated is generally wanted the electric heating system of supporting vacuum air compression machine and stoste material, the electric energy that extra consumption is more.Though the vacuum in the degasser tank body and the temperature of stoste material can have influence on the effect of the degassing; But, in production practices, can know that through repeatedly testing the vacuum in the tank body need not very high; The stoste material also needn't be awfully hot, just can reach the purpose that the stoste material is fully outgased.So can obtain vacuum and heating stoste material in the above-mentioned tank body with other comparatively easy method fully.
Summary of the invention
The purpose of the utility model provides and a kind ofly vacuumizes and the degasser of double as heating heating agent with steam, and the corollary system that overcomes present vacuum degassing machine is complicated, will consume more deficiencies such as electric energy.
The utility model is achieved through following technical proposals.
The utility model comprises tank body, charging aperture, dehvery pump, conveying pipeline, control valve and injection spray pipe; Be provided with boiler, the feed liquid heating tube be housed in it, the import of said feed liquid heating tube through said conveying pipeline be communicated with the outlet of said dehvery pump, its outlet is communicated with said injection spray pipe through said conveying pipeline and said control valve; Steam jet ejector is equipped with on top in said tank body; Said steam jet ejector is communicated with the inner chamber of said tank body through air intake duct and suction modulation; The air intake of said steam jet ejector is connected with steam supply pipe and steam supply valve, its venthole are equipped with steam reuse pipe, and the outlet of said steam reuse pipe is stretched into said boiler and immersed in the water.In the utility model, utilize said boiler that the stoste material is heated, utilize said steam jet ejector to come said tank body is vacuumized.From coordinative composition of equipments, simpler and easy than electric heater and vacuum air compression machine, from the energy that consumes, be than low other steam ability of level of electric energy.What have more positive effect is: the one, utilize the kinetic energy of steam by said steam jet ejector, and utilize the heat of steam by said boiler, steam fully is utilized; The 2nd, can utilize some " tail vapour " " the surplus vapour " in the food processing enterprises, because the production equipment that needs high temperature and high pressure steam is all arranged in the general food processing enterprises, these production equipments often have a lot " tail vapour " " surplus vapour " by utilization well.In order to improve the heat-transfer effect of said feed liquid heating tube, fin is equipped with in the outside of said feed liquid heating tube; Can said feed liquid heating tube be spiral coil also.Therefore the temperature of said boiler and said steam reuse tube-surface can, be provided with heat-insulation layer in the outside of said boiler and said steam reuse pipe than higher, can avoid the careless scald of operator to also help energy-conservation like this.Water inlet pipe, water intaking valve and drainpipe, draining valve are housed on the said boiler.
Against existing technologies, the beneficial effect of the utility model is:
Simplified the corollary system of vacuum degasser, utilized, improved the utilization rate of steam,, helped energy-conservation also for to utilize the steam " tail vapour " " surplus vapour " of enterprises to create condition than the low-level energy of electric energy.
Description of drawings
Accompanying drawing is the structural representation of the utility model (said feed liquid heating tube is a spiral coil), among the figure: 1 tank body, 2, charging aperture, 3, dehvery pump, 4, conveying pipeline; 5, control valve, 6, injection spray pipe, 7 boilers, 8, the feed liquid heating tube, 9, steam jet ejector; 10, air intake duct, 11, suction modulation, 12, steam supply pipe, 13, steam supply valve, 14, steam reuse pipe; 15, heat-insulation layer, 16, water inlet pipe, 17, water intaking valve, 18, drainpipe, 19, draining valve.
The specific embodiment
Below in conjunction with the accompanying drawing and the specific embodiment the utility model is done further to describe.
Conveying feed liquid part during this practicality is new, spraying part, tank body part are prior art.Steam jet ejector also is the product of a maturation, uses morely in fields such as air conditioner refrigeratings, and the utility model can be selected the finished product of less model for use, also can self manufacture.Steam reuse pipe 14 should be selected the bigger pipeline of internal diameter for use, can reduce the resistance of steam in pipeline like this, guarantees that steam jet ejector 9 can produce enough negative pressure, and the flow velocity of steam is diminished, and reduces noise in the time of in the water in leaking into boiler 7.When the utility model uses: open steam supply valve 13 earlier, steam promptly through steam supply pipe 12 at a high speed through steam jet ejector 9, after enter in the boiler; Open suction modulation 11 again, adjust the vacuum in the tank body 1.At this moment, just can open dehvery pump 3 and align control valve 5, feed liquid is just flowed into by charging aperture 2, after the heating through feed liquid heating tube 8 is able to heat up, is sprayed into vaporific at injection spray pipe 6; The gas that is contained in the feed liquid is removed fully.
Claims (4)
1. one kind vacuumizes with steam and the degasser of double as heating heating agent; Comprise tank body, charging aperture, dehvery pump, conveying pipeline, control valve and injection spray pipe; It is characterized in that; Be provided with boiler, the feed liquid heating tube be housed in it, the import of said feed liquid heating tube through said conveying pipeline be communicated with the outlet of said dehvery pump, its outlet is communicated with said injection spray pipe through said conveying pipeline and said control valve; Steam jet ejector is equipped with on top in said tank body; Said steam jet ejector is communicated with the inner chamber of said tank body through air intake duct and suction modulation; The air intake of said steam jet ejector is connected with steam supply pipe and steam supply valve, its venthole are equipped with steam reuse pipe, and the outlet of said steam reuse pipe is stretched into said boiler and immersed in the water.
2. a kind ofly vacuumize and the degasser of double as heating heating agent according to claim 1 is said, it is characterized in that fin is equipped with in the outside of said feed liquid heating tube with steam.
3. a kind ofly vacuumize and the degasser of double as heating heating agent according to claim 1 is said, it is characterized in that said feed liquid heating tube is a spiral coil with steam.
4. a kind ofly vacuumize and the degasser of double as heating heating agent according to claim 1 is said, it is characterized in that the outside of said boiler and said steam reuse pipe is provided with heat-insulation layer with steam.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120573144 CN202425565U (en) | 2011-12-26 | 2011-12-26 | Degasser using steam for evacuation and as heating medium |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201120573144 CN202425565U (en) | 2011-12-26 | 2011-12-26 | Degasser using steam for evacuation and as heating medium |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202425565U true CN202425565U (en) | 2012-09-12 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201120573144 Expired - Fee Related CN202425565U (en) | 2011-12-26 | 2011-12-26 | Degasser using steam for evacuation and as heating medium |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202425565U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107961564A (en) * | 2017-12-08 | 2018-04-27 | 安徽清华农业发展有限公司 | A kind of new beverage vacuum degassing machine |
| CN108402378A (en) * | 2018-04-18 | 2018-08-17 | 德清秋水果汁有限公司 | A kind of fruit juice degasser |
-
2011
- 2011-12-26 CN CN 201120573144 patent/CN202425565U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107961564A (en) * | 2017-12-08 | 2018-04-27 | 安徽清华农业发展有限公司 | A kind of new beverage vacuum degassing machine |
| CN108402378A (en) * | 2018-04-18 | 2018-08-17 | 德清秋水果汁有限公司 | A kind of fruit juice degasser |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120912 Termination date: 20121226 |