CN203763913U - Degasser - Google Patents
Degasser Download PDFInfo
- Publication number
- CN203763913U CN203763913U CN201420156981.4U CN201420156981U CN203763913U CN 203763913 U CN203763913 U CN 203763913U CN 201420156981 U CN201420156981 U CN 201420156981U CN 203763913 U CN203763913 U CN 203763913U
- Authority
- CN
- China
- Prior art keywords
- degassing tank
- degasser
- furnished
- cooling water
- degassing
- 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 - Lifetime
Links
- 238000007872 degassing Methods 0.000 claims abstract description 64
- 238000007599 discharging Methods 0.000 claims abstract description 34
- 238000011084 recovery Methods 0.000 claims abstract description 20
- 238000009833 condensation Methods 0.000 claims abstract description 12
- 230000005494 condensation Effects 0.000 claims abstract description 12
- 239000000498 cooling water Substances 0.000 claims description 25
- 239000003205 fragrance Substances 0.000 claims description 8
- 238000004140 cleaning Methods 0.000 claims description 5
- 239000003599 detergent Substances 0.000 claims description 5
- 238000007600 charging Methods 0.000 claims description 3
- 230000002000 scavenging effect Effects 0.000 claims description 3
- 239000000126 substance Substances 0.000 abstract description 12
- 125000003118 aryl group Chemical group 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 10
- 239000007788 liquid Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- 235000013361 beverage Nutrition 0.000 description 5
- 239000002826 coolant Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 239000000796 flavoring agent Substances 0.000 description 4
- 235000019634 flavors Nutrition 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 235000013305 food Nutrition 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000006701 autoxidation reaction Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000009849 vacuum degassing Methods 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
Abstract
The utility model relates to a degasser. The degasser comprises a degassing assembly (1) and an aromatic recovery assembly (2), wherein the degassing assembly (1) consists of a degassing tank (11) and a discharging pump (12), the degassing tank (11) is fed through a feeding pipeline (3), the bottom is connected with a discharging pump (12) through a discharging pipeline (4), wherein the aromatic recovery assembly (2) comprises a condensation pipe (21), a recovery pipe (22) and a vacuum pump (23), one end of the condensation pipe (21) is connected with the top of the degassing tank (11), the other end of the condensation pipe (21) is connected with the side wall of the recovery pipe (22), the top of the recovery pipe (22) is connected with the vacuum pump (23), and the bottom of the recovery pipe (22) is connected with the discharging pipeline (4). The degasser provided by the utility model also has the function of recovering aromatic substances on the basis of guaranteeing the degassing efficiency and degassing effect, and is simple in structure, diversified in functions, and convenient to operate.
Description
Technical field
The utility model relates to a kind of degasser, especially a kind of degasser for food and drink degassing process.
Background technology
In industrial production, particularly, in food_beverage industry, usually to carry out degassing process to liquid, be mainly to slough oxygen wherein etc., avoid liquid autoxidation in storage process, extend its pot-life.Degasser generally comprises degassing tank, vavuum pump and discharging pump.Vavuum pump makes to produce vacuum in degassing tank, needs degassed liquid to be entered after degassing tank by feed pipe, sloughs in liquid the gases such as dissolved oxygen, then by the discharging pump being connected with degassing tank bottom, is transported in storage tank.
As China Patent No. ZL95221444.X, disclose and a kind of liquid has been carried out to vacuum filtration and degassed device.Existing filter and degasser are all independently to install, and must have pumping power separately, need to arrange temporary basin between when stream oriented device is connected.This device is connected filtering bodies filtrate (liquid with vacuum tank, the import of vacuum tank discharging opening and discharging pump is joined, and makes to filter and degassed becoming one, and utilizes vacuum when degassed as filtering power, thereby reduces power consumption, equipment is taken up an area little, cost saving.
On the basis of traditional degasser, by the shower nozzle of feed pipe is improved to wall-flow type shower nozzle, can effectively improve degassing efficiency and degasifying effect.
As China Patent No. ZL201010617821.1, a kind of wall-flow type vacuum degassing machine and circulating fluid automatic deaerating method are disclosed, constraining in the liquid that circulates under pressure penetrates along the inwall of closed container, gas departs from liquid and discharges from container center region, belong to liquid-circulating application, a kind of liquid-circulating low level exhaust technique, can extensive use and various liquid-circulating occasion, can realize product seriation, standardization, generalization and produce.
In above-mentioned technology, although guaranteed degassing efficiency and degasifying effect, in liquid, many useful components also very easily volatilize away in vacuum environment, cause the loss on composition.But, if reduce vacuum, make conversely again the liquid cannot be fully degassed, reduced degasifying effect.So, need on the basis of existing degasser, add retracting device.
As China Patent No. ZL94218275.8, a kind of collecting-type degasting equipment is disclosed, the gas mixing for removing fluid foods, is mainly comprised of membrane degassing tank, collection type condenser and collector.Fluid foods is sprayed into film in the membrane degassing tank of vacuum, has fully strengthened leaving area; The gas of discharging and part solid particle are introduced collection type condenser by Vacuum exhaust tube, through centrifugation, cooling water condensation and steps of exhausting collect the material component losing in degasification process again, maintain to greatest extent original composition of material, solved the problem that when degassing equipment is degassed in the past, material component is also lost.
The material component of degassing process is recovered in food_beverage industry and is even more important, due to the most highly volatile of the aromatic substance in beverage.If loss in a large number, causes beverage to lose original local flavor in degasification process, can greatly reduce the market attractiveness of product.It is particularly necessary that degasser in food_beverage industry installs retracting device additional.
As China Patent No. ZL201210406285.X, former zestful liquid beverage of a kind of maintenance and preparation method thereof is disclosed, particularly a kind of product that reduces the loss of product processing flavor substances by physical method and technology controlling and process and preparation method thereof.Preferred employing deoxidation---fragrance reclaim---aromatic substance returns and adds technology and equipment by liquid beverage of the online Hui Tian of aromatic substance losing in process and preparation method thereof.The present invention has successfully solved the collection of losing flavor substance in liquid beverage process, concentrated and Hui Tian, makes product retain to greatest extent the original local flavor of product.
Although technique scheme has proposed effective solution for different problems, but there is function singleness, complex structure and other problems, a kind of degasser that is applied to food_beverage industry need to be provided, guaranteeing, on the basis of degassing efficiency and degasifying effect, to there is again the function that reclaims aromatic substance simultaneously.
Summary of the invention
Technical problem to be solved in the utility model is to provide a kind of degasser, is guaranteeing, on the basis of degassing efficiency and degasifying effect, to have again the function that reclaims aromatic substance simultaneously.
The utility model solves the problems of the technologies described above taked technical scheme: a kind of degasser, comprise that degassed assembly and fragrance reclaim assembly, wherein, degassed assembly is comprised of degassing tank and discharging pump, degassing tank is by feeding pipe charging, bottom is connected by discharging pipeline with discharging pump, fragrance reclaims assembly and comprises condenser pipe, recovery tube and vavuum pump, it is characterized in that: described condenser pipe one end is connected with degassing tank top, the other end is connected with recovery tube sidewall, recovery tube top is connected with vavuum pump, and bottom is connected with discharging pipeline.
On the basis of such scheme, the tube wall of described condenser pipe has the condensate layer of cooling water that can circulate, and is furnished with condenser pipe cooling water inlet and condenser pipe coolant outlet.
On the basis of such scheme, described condensing tube condensation layer and degassing tank top are additionally connected with detergent line, and are furnished with cleaning shower nozzle, and described discharging pump is furnished with scavenging pump.
On the basis of such scheme, the bottom tube wall of described degassing tank has the degassing tank condensate layer of the cooling water that can circulate, and is furnished with degassing tank cooling water intake and degassing tank cooling water outlet.
On the basis of such scheme, described feeding pipe is tangentially connected to degassing tank sidewall, and is furnished with wall-flow type shower nozzle.
On the basis of such scheme, the described feeding pipe other end is connected with filter discharging opening.
On the basis of such scheme, described vavuum pump is furnished with Air-regulating valves.
The utility model has the advantage of: guaranteeing, on the basis of degassing efficiency and degasifying effect, to there is again the function that reclaims aromatic substance simultaneously; Simple in structure, diverse in function, easy to operate.
Accompanying drawing explanation
Fig. 1 is the stereogram of the utility model specific embodiment;
Fig. 2 is work schematic diagram of the present utility model;
Fig. 3 is the front view of the utility model specific embodiment;
Fig. 4 is the left view of the utility model specific embodiment;
Fig. 5 is the top view of the utility model specific embodiment;
Fig. 6 is the front view of the utility model degassing tank;
Attached number in the figure explanation:
1---degassed assembly;
11---degassing tank; 111---degassing tank condensate layer;
112---degassing tank cooling water intake; 113---degassing tank cooling water outlet;
12---discharging pump; 121---scavenging pump;
2---fragrance reclaims assembly; 21---condenser pipe;
211---condenser pipe cooling water intake; 212---condenser pipe cooling water outlet;
22---recovery tube;
23---vavuum pump; 231---Air-regulating valves;
3---feeding pipe; 31---wall-flow type shower nozzle;
4---discharging pipeline;
5---detergent line; 51---clean shower nozzle.
The specific embodiment
Referring to stereogram, Fig. 2 that Fig. 1 is the utility model specific embodiment and be work schematic diagram of the present utility model, Fig. 3 and be the front view of the utility model specific embodiment, the left view that Fig. 4 is the utility model specific embodiment, top view and Fig. 6 that Fig. 5 is the utility model specific embodiment is the front view of the utility model degassing tank:
As shown in Figures 1 to 5, a kind of degasser, comprise that degassed assembly 1 and fragrance reclaim assembly 2, wherein, degassed assembly 1 is comprised of degassing tank 11 and discharging pump 12, degassing tank 11 is by feeding pipe 3 chargings, bottom is connected by discharging pipeline 4 with discharging pump 12, fragrance reclaims assembly 2 and comprises condenser pipe 21, recovery tube 22 and vavuum pump 23, wherein: described condenser pipe 21 one end are connected with degassing tank 11 tops, the other end is connected with recovery tube 22 sidewalls, and recovery tube 22 tops are connected with vavuum pump 23, and bottom is connected with discharging pipeline 4.
Before use, with vavuum pump 23 by degassing tank 11, condenser pipe 21 and recovery tube 22 state that is evacuated, material enters degassing tank 11 from feeding pipe 3, after gas-liquid separation, material after degassed enters discharging pump 12 by discharging pipeline 4, and gases such as oxygen of extracting out and together enter condenser pipe 21 with aromatic substance steam, after condensation, with aromatic substance steam, be again condensed into liquid, separated from the gas, enter after recovery tube, gas is discharged from recovery tube 22 tops, and the aromatic substance of recovery is got back in discharging pipeline 4.
On the basis of such scheme, as depicted in figs. 1 and 2, the tube wall of described condenser pipe 21 has the condensing tube condensation layer of the cooling water that can circulate, and is furnished with condenser pipe cooling water inlet 211 and condenser pipe coolant outlet 212.
Open condenser pipe cooling water inlet 211, cooling water enters condensing tube condensation layer, plays the effect of condensation, and condenser pipe coolant outlet 212 is for controlling water level.
On the basis of such scheme, the condensate layer of described condenser pipe 21 and degassing tank 11 tops are additionally connected with detergent line 5, and are furnished with the shower nozzle 51 of cleaning, and described discharging pump 12 is furnished with scavenging pump 121.
Degasser after hours, cuts out coolant outlet 212, and cooling water is sprayed in degassing tank 11 by the cleaning shower nozzle 51 of detergent line 5, and matching purge pump 121, for cleaning degassing tank 11, discharging pipeline 4 and discharging pump 12.
On the basis of such scheme, described feeding pipe 3 other ends are connected with filter discharging opening.
Filter and degasser are simply combined into one, utilize the pump pressure of degasser to drive the liquid in filter, reduce cost.
On the basis of such scheme, as shown in Figure 2, described vavuum pump 23 is furnished with Air-regulating valves 231.
Air-regulating valves 231 is for regulating the vacuum state of degasser.
As shown in Figure 6, on the basis of such scheme, the bottom tube wall of described degassing tank 11 has the degassing tank condensate layer 111 of the cooling water that can circulate, and is furnished with degassing tank cooling water intake 112 and degassing tank cooling water outlet 113.
Open degassing tank cooling water inlet 112, cooling water enters degassing tank condensate layer 111, plays the effect of condensation, and coolant outlet 113 is for controlling water level.
On the basis of such scheme, described feeding pipe 3 is tangentially connected to degassing tank 11 sidewalls, and is furnished with wall-flow type shower nozzle 31.
Wall-flow type shower nozzle 31 can effectively improve degassing efficiency and the degasifying effect of degasser.
Claims (7)
1. a degasser, comprise that degassed assembly (1) and fragrance reclaim assembly (2), wherein, degassed assembly (1) is comprised of degassing tank (11) and discharging pump (12), degassing tank (11) is by feeding pipe (3) charging, bottom is connected by discharging pipeline (4) with discharging pump (12), it is characterized in that: described fragrance reclaims assembly (2) and comprises condenser pipe (21), recovery tube (22) and vavuum pump (23), described condenser pipe (21) one end is connected with degassing tank (11) top, the other end is connected with recovery tube (22) sidewall, recovery tube (22) top is connected with vavuum pump (23), bottom is connected with discharging pipeline (4).
2. degasser according to claim 1, it is characterized in that: the tube wall of described condenser pipe (21) has the condensing tube condensation layer of the cooling water that can circulate, and be furnished with condenser pipe cooling water intake (211) and condenser pipe cooling water outlet (212).
3. degasser according to claim 2, it is characterized in that: described condensing tube condensation layer and degassing tank (11) top are additionally connected with detergent line (5), and be furnished with cleaning shower nozzle (51), described discharging pump (12) is furnished with scavenging pump (121).
4. degasser according to claim 1, is characterized in that: the bottom tube wall of described degassing tank (11) has degassing tank condensate layer (111), and is furnished with degassing tank cooling water intake (112) and degassing tank cooling water outlet (113).
5. degasser according to claim 1, is characterized in that: described feeding pipe (3) is tangentially connected to degassing tank (11) sidewall, and is furnished with wall-flow type shower nozzle (31).
6. degasser according to claim 1, is characterized in that: described feeding pipe (3) other end is connected with filter discharging opening.
7. degasser according to claim 1, is characterized in that: described vavuum pump (23) is furnished with Air-regulating valves (231).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420156981.4U CN203763913U (en) | 2014-04-02 | 2014-04-02 | Degasser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420156981.4U CN203763913U (en) | 2014-04-02 | 2014-04-02 | Degasser |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203763913U true CN203763913U (en) | 2014-08-13 |
Family
ID=51281162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420156981.4U Expired - Lifetime CN203763913U (en) | 2014-04-02 | 2014-04-02 | Degasser |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203763913U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104548670A (en) * | 2014-12-25 | 2015-04-29 | 东莞埃欧热能技术有限公司 | Vacuum degassing tank |
| CN106975244A (en) * | 2017-03-10 | 2017-07-25 | 洁翼流体技术（上海）有限公司 | A kind of degassing equipment in the production for milk beverage |
| 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 |
| CN108342300A (en) * | 2018-05-18 | 2018-07-31 | 江西省食品发酵研究所 | A kind of fermentation machine for adjusting back fermentation temperature |
-
2014
- 2014-04-02 CN CN201420156981.4U patent/CN203763913U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104548670A (en) * | 2014-12-25 | 2015-04-29 | 东莞埃欧热能技术有限公司 | Vacuum degassing tank |
| CN106975244A (en) * | 2017-03-10 | 2017-07-25 | 洁翼流体技术（上海）有限公司 | A kind of degassing equipment in the production for milk beverage |
| 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 |
| CN108342300A (en) * | 2018-05-18 | 2018-07-31 | 江西省食品发酵研究所 | A kind of fermentation machine for adjusting back fermentation temperature |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140813 |
|
| CX01 | Expiry of patent term |