CN104548670A - Vacuum degassing tank - Google Patents
Vacuum degassing tank Download PDFInfo
- Publication number
- CN104548670A CN104548670A CN201410830758.8A CN201410830758A CN104548670A CN 104548670 A CN104548670 A CN 104548670A CN 201410830758 A CN201410830758 A CN 201410830758A CN 104548670 A CN104548670 A CN 104548670A
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- tank body
- exchange core
- passage
- plate journey
- 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.)
- Granted
Links
Landscapes
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The invention discloses a vacuum degassing tank. The vacuum degassing tank comprises a tank body, and a feed liquid inlet and a feed liquid outlet which are formed in the tank body, wherein a flange is arranged at the upper end of the tank body; a demountable condenser assembly is mounted on the flange; the condenser assembly comprises a shell mounted at the upper end of the tank body, and a first heat exchange core and a second heat exchange core which are mounted in the shell and are connected with each other in parallel; a first plate side channel and a second shell side channel which are isolated with each other are arranged in the first heat exchange core; a second plate side channel and a second shell side channel which are isolated with each other are arranged in the second heat exchange core; the first plate side channel is communicated with the second plate side channel; the first shell side channel is communicated with an inner cavity of the shell and the second shell side channel; the lower end of the second heat exchange stretches into an inner cavity of the tank body, so that the second shell side channel is communicated with the inner cavity of the tank body; a vacuumizing hole communicated with the first shell side channel is formed in the shell. The vacuum degassing tank has an excellent degassing effect and an excellent heat exchange effect, is simple and convenient to use and convenient to repair and maintain, and has high market competitiveness.
Description
Technical field:
The present invention relates to degassing tank product technical field, refer in particular to a kind of vacuum receiver.
Background technology:
Vacuum receiver is the device utilizing vacuum draw effect to get rid of contained incoagulable gas in feed liquid, be one is degassed requisite equipment on the feed liquid such as dairy products, fruit juice production line.The effect of vacuum receiver is: remove the air (oxygen) in feed liquid, and the oxidation of Restrain browning, pigment, vitamin, fragrant composition and other materials, prevents quality from reducing; Removal is attached to outstanding loose particulate gas in feed liquid, suppresses particulate to float, keeps good appearance; Preventing bubbles when canned and high temperature sterilization affects sterilization; Reduce the corrosion to container inner wall.
Current most degassing tank operation principle is: at the temperature of 55-65 DEG C, adopt nozzle to spray in degassing tank by feed liquid, and due under vacuum conditions, boiling point reduces, feed liquid boiling vaporization.At this moment, the oxygen (air) contained in feed liquid and aroma gases evaporate, and gas, toward rising, after filter screen stops, is taken away by vavuum pump, directly drained.
Above-mentioned degassing tank comes with some shortcomings, just directly taken away by vavuum pump because the oxygen (air) that contains in feed liquid and aroma gases are just stopped by filter screen after evaporating, now, moisture in oxygen (air) and aroma gases can be taken away by vavuum pump too, waste can be caused like this, and the work quality of vavuum pump can be affected, in addition, the temperature of oxygen (air) and aroma gases is still higher, it is directly pumped, so that waste heat energy, and the degasifying effect of degassing tank can be affected.
Summary of the invention:
The object of the invention is to overcome the deficiencies in the prior art, a kind of vacuum receiver is provided.
In order to solve the problems of the technologies described above, present invention employs following technical proposals: this vacuum receiver comprises tank body, be arranged at the liquor inlet on tank body and material liquid outlet, described tank body upper end is provided with a flange, in this flange, removable condenser assembly is installed, this condenser assembly comprises: be installed on the housing of tank body upper end and be installed on the first heat exchange core in housing and parallel with one another and the second heat exchange core, there is in this first heat exchange core the first mutually isolated plate journey passage and the first shell side passage, this second heat exchange core has the second mutually isolated plate journey passage and the second shell side passage, wherein, first plate journey passage and the second plate journey channel connection, first shell side passage and housing cavity and the second shell side channel connection, described second heat exchange core lower end is stretched in tank inner chamber, make the second shell side channel connection tank inner chamber, and this housing is provided with the vacuum orifice with the first shell side channel connection.
Furthermore, in technique scheme, described housing is provided with a medium and goes out pipe and be installed on medium to go out medium inlet pipe in pipe and mutually isolated, makes medium go out pipe and forms tube-in-tube structure with medium inlet pipe; Wherein, medium inlet pipe lower port respectively with the inlet communication of described first plate journey passage and the second plate journey passage, medium go out infratubal port respectively with the outlet of the first plate journey passage and the second plate journey passage.
Furthermore, in technique scheme, form stable assembling by the forward and backward baffle plate bar that is connected between the first described heat exchange core and the second heat exchange core, wherein, between the first heat exchange core and the second heat exchange core, be formed with interval.
Furthermore, in technique scheme, described forward and backward baffle plate periphery is provided with the first spoiler and the second spoiler, wherein, first spoiler and the second spoiler lay respectively at the first heat exchange core and the second heat exchange core is peripheral, and the second spoiler is installed on the flange of tank body upper end, the first spoiler outer rim and inner walls are closely conflicted.
Furthermore, in technique scheme, described front apron is provided with respectively with first, second body of the inlet communication of the first plate journey passage and the second plate journey passage, described medium inlet pipe lower port is communicated with first, second body by the first tube connector; Described backboard is provided with respectively with the 3rd, the 4th body of the outlet of the first plate journey passage and the second plate journey passage, described medium is gone out infratubal port and is communicated with by the second tube connector and the 3rd, the 4th body.
Furthermore, in technique scheme, the internal diameter of described first, second, third, fourth body is all consistent; First, second tube connector internal diameter size described is twice of the first internal diameter of tube body size or more, and this first and second tube connector end all has a reducing linkage section, and is connected with the second body and the 4th body respectively by this linkage section.
Furthermore, in technique scheme, described vacuum orifice inside is also provided with one first cleaning mouthpiece, and this first cleaning mouthpiece lower end is stretched in housing cavity, and this first cleaning mouthpiece lower end is provided with the first shower nozzle.
Furthermore, in technique scheme, described tank body is provided with one second cleaning mouthpiece, this second cleaning mouthpiece end is stretched in the middle part of tank inner chamber, and this second cleaning mouthpiece end is provided with the second shower nozzle.
Furthermore, in technique scheme, described tank body is provided with the form of at least one observable tank inner chamber situation.
Furthermore, in technique scheme, described tank body is provided with capacitance liquid level meter interface, in this capacitance liquid level meter interface, capacitance liquid level meter is installed; Described tank body lower end is provided with the feet of at least three horizon adjustables.
After adopting technique scheme, the present invention has following beneficial effect compared with prior art:
1, because condenser assembly in the present invention adopts two-stage heat exchange core to carry out heat exchange, so that reach fabulous condensation effect, can effectively improve degasifying effect of the present invention, in addition, also flow back under gravity in tank body because the condensate moisture in fragrance or oxygen (air) is become liquid by condenser assembly, so that unnecessary waste can not be caused, and the work quality of vavuum pump can not be affected; In addition, oxygen (air) temperature after heat exchange taken away by vavuum pump is all lower, to cause heat to be effectively utilized, can effectively improve the market competitiveness of the present invention.
2, removed moisture content by the oxygen (air) that vavuum pump is taken away, that not only reduces system has oxygen corrosion, extension device service time, also can time condenser assembly surface can not have gas bubbles, improve the heat exchange efficiency of condenser assembly.
3, the condenser assembly in the present invention and tank body are modularized design, use simpler, and can fully automatic operation, safe and reliable, for ease of maintenaince maintain.
Accompanying drawing illustrates:
Fig. 1 is stereogram of the present invention;
Fig. 2 is perspective view of the present invention;
Fig. 3 is top view of the present invention;
Fig. 4 is the stereogram of condenser assembly in the present invention;
Fig. 5 is the internal structure schematic diagram of condenser assembly in the present invention.
Detailed description of the invention:
Below in conjunction with specific embodiments and the drawings, the present invention is further described.
See shown in Fig. 1-5, be a kind of vacuum receiver, comprise tank body 1, be arranged at liquor inlet 11 on tank body 1 and material liquid outlet 12 and removable condenser assembly 2.
Described condenser assembly 2 is arranged at tank body 1 top, and after feed liquid boiling, evaporation rises to tank body 1 top, and enters condenser assembly 2 in time and carry out condensation, can Loss reducing.
Described tank body 1 upper end is provided with a flange, is provided with described condenser assembly 2 in this flange, and this condenser assembly 2 comprises: be installed on the housing 21 of tank body 1 upper end and be installed on the first heat exchange core 22 and the second heat exchange core 23 in housing 21 and parallel with one another.
The flange that described housing 21 adopts chase mortise face to seal with tank body 1 upper end, that is, flange sealing surface is chase mortise formula, and air-tightness is good, and dismounting is convenient, easy to clean.
There is in described first heat exchange core 22 the first mutually isolated plate journey passage and the first shell side passage, specifically, this first heat exchange core 22 comprises organizes plate groups more, often organize plate groups and comprise two panels plate, wherein, be formed with one first ripple gap between adjacent two plate groups, this first ripple matched in clearance housing 21 inwall forms the first described shell side passage; Form the second ripple gap isolated with described first shell side passage between two panels plate in described plate groups, this second ripple gap is as the first described plate journey passage.
The plate that described first heat exchange core 22 inside uses is corrugated cardboard sheet, and the ripple on plate not only improves the turbulent extent of fluid, and forms many contact points, to bear normal operating pressure.Corrugated cardboard sheet can make turbulivity uprise, and high turbulent flow can also give full play to cleaning action, effectively dirt deposits can be reduced to minimum, makes heat transfer effect reach best.
Described second heat exchange core 23 has the second mutually isolated plate journey passage and the second shell side passage, and the structure of this second heat exchange core 23 is consistent with the structure of above-mentioned first heat exchange core 22, and this is no longer going to repeat them.
Described first plate journey passage and the second plate journey channel connection, first shell side passage and housing 21 inner chamber and the second shell side channel connection, described second heat exchange core 23 lower end is stretched in tank body 1 inner chamber, make the second shell side channel connection tank body 1 inner chamber, and this housing 21 is provided with the vacuum orifice 13 with the first shell side channel connection.
Described housing 21 is provided with a medium and goes out pipe 211 and be installed on medium to go out medium inlet pipe 212 in pipe 211 and mutually isolated, makes medium go out pipe 211 and forms tube-in-tube structure with medium inlet pipe 212; Wherein, medium inlet pipe 212 lower port respectively with the inlet communication of described first plate journey passage and the second plate journey passage, medium go out pipe 211 lower port respectively with the outlet of the first plate journey passage and the second plate journey passage.
Stable assembling is formed by forward and backward baffle plate 24,25 bar 26 that is connected between the first described heat exchange core 22 and the second heat exchange core 23, wherein, be formed with interval between first heat exchange core 22 and the second heat exchange core 23, the first plate journey passage in the first heat exchange core 22 can be quickly flowed into cause the gas flowed through in the second heat exchange core 23 after second plate journey passage.Described forward and backward baffle plate 24,25 periphery is provided with the first spoiler 241 and the second spoiler 242, wherein, first spoiler 241 and the second spoiler 242 lay respectively at the first heat exchange core 22 and the second heat exchange core 23 is peripheral, and the second spoiler 242 is installed on the flange of tank body 1 upper end, the first spoiler 241 outer rim and housing 21 inwall are closely conflicted.
Described front apron 24 is provided with respectively with first, second body 221,231 of the inlet communication of the first plate journey passage and the second plate journey passage, described medium inlet pipe 212 lower port is communicated with first, second body 221,231 by the first tube connector 213; Described backboard 25 is provided with respectively with the 3rd, the 4th body 222,232 of the outlet of the first plate journey passage and the second plate journey passage, described medium is gone out pipe 211 lower port and is communicated with by the second tube connector 214 and the 3rd, the 4th body 222,232.Wherein, the internal diameter of described first, second, third, fourth body 221,231,222,232 is all consistent; First, second tube connector 213,214 internal diameter size described is twice of the first body 221 internal diameter size or more, and this first and second tube connector 213,214 end all has a reducing linkage section, and be connected with the second body 231 and the 4th body 232 respectively by this linkage section.
Described vacuum orifice 13 inside is also provided with one first cleaning mouthpiece 14, this the first cleaning mouthpiece 14 lower end is stretched in housing 21 inner chamber, and this first cleaning mouthpiece 14 lower end is provided with the first shower nozzle, this first cleaning mouthpiece 14 is by flowing into cleaning fluid to clean condenser assembly 2.
Described tank body 1 is provided with one second cleaning mouthpiece 15, this the second cleaning mouthpiece 15 end is stretched in the middle part of tank body 1 inner chamber, and this second cleaning mouthpiece 15 end is provided with the second shower nozzle, this second cleaning mouthpiece 15 is by flowing into cleaning fluid to clean tank body 1.
Described tank body 1 is provided with the form 16 of at least one observable tank body 1 inner chamber situation, so that in use, staff can observe tank body 1 inner chamber situation the moment, operates safer.
Described tank body 1 is provided with capacitance liquid level meter interface 17, in this capacitance liquid level meter interface 17, capacitance liquid level meter is installed; Described tank body 1 lower end is provided with the feet 18 of at least three horizon adjustables.
The present invention in use, ensures that the vacuum in tank body 1 is-0.45 ~-0.65bar, sprays into tank body 1 by 55 ~ 65 DEG C of feed liquids from medium inlet pipe 212, and due under the vacuum environment in tank body 1, boiling point reduces, feed liquid boiling vaporization.At this moment the oxygen (air) contained in feed liquid and aroma gases evaporate, gas is toward rising, then through condenser assembly 2, the condensate moisture in fragrance or oxygen (air) is become liquid also to flow back under gravity in tank body, feed liquid finally goes out pipe 211 from medium and flows out, and vacuum orifice 13 connects vavuum pump by oxygen (air) takes away, directly drain.
When gas flows to condenser assembly 2, two-stage heat exchange can be carried out, gas is forced to the second shell side passage entering the second heat exchange core 23 from the bottom up under the stop of the second spoiler 242, one-level heat exchange is realized with the refrigerant in the second plate journey passage of heat exchange core 23, flow through the gas after the second shell side passage of the second heat exchange core 23 and again stopped the first shell side passage being forced to enter from the bottom up the first heat exchange core 22 by the first spoiler 241, realize secondary heat exchange with the refrigerant in the first plate journey passage of heat exchange core 23.Meanwhile, cold medium is poured into from medium inlet pipe 212, and after flowing through the first plate journey passage of the first heat exchange core 22 and the second plate journey passage of the second heat exchange core 23 respectively, converge and flow to medium and go out pipe 211, and go out pipe 211 from medium and flow out, so just can enable to flow to oxygen (air) in condenser assembly 2 and aroma gases effectively carries out heat exchange with the cold medium flow in condenser assembly 2, liquid state is become also to flow back under gravity in tank body the condensate moisture in fragrance or oxygen (air) to cause through condenser assembly 2, and on-condensible gas is evacuated mouth 13 connects vavuum pump and take away, make the effect that degassing tank reaches degassed.
Because condenser assembly in the present invention 2 adopts two-stage heat exchange core to carry out heat exchange, so that reach fabulous condensation effect, can effectively improve degasifying effect of the present invention, in addition, also flow back under gravity in tank body because the condensate moisture in fragrance or oxygen (air) is become liquid by condenser assembly 2, so that unnecessary waste can not be caused, and the work quality of vavuum pump can not be affected; In addition, oxygen (air) temperature after heat exchange taken away by vavuum pump is all lower, to cause heat to be effectively utilized, can effectively improve the market competitiveness of the present invention.
Removed moisture content by the oxygen (air) that vavuum pump is taken away, that not only reduces system has oxygen corrosion, extension device service time, also can time condenser assembly surface can not have gas bubbles, improve the heat exchange efficiency of condenser assembly.
Condenser assembly in the present invention and tank body are modularized design, use simpler, and can fully automatic operation, safe and reliable, for ease of maintenaince maintain.
Certainly, the foregoing is only specific embodiments of the invention, be not limit the scope of the present invention, all equivalences done according to structure, feature and principle described in the present patent application the scope of the claims change or modify, and all should be included in the present patent application the scope of the claims.
Claims (10)
1. a vacuum receiver, comprises tank body (1), is arranged at liquor inlet (11) on tank body (1) and material liquid outlet (12),
It is characterized in that: described tank body (1) upper end is provided with a flange, in this flange, removable condenser assembly (2) is installed, this condenser assembly (2) comprising: be installed on the housing (21) of tank body (1) upper end and be installed on the first heat exchange core (22) in housing (21) and parallel with one another and the second heat exchange core (23), there is in this first heat exchange core (22) the first mutually isolated plate journey passage and the first shell side passage, this second heat exchange core (23) has the second mutually isolated plate journey passage and the second shell side passage, wherein, first plate journey passage and the second plate journey channel connection, first shell side passage and housing (21) inner chamber and the second shell side channel connection, described second heat exchange core (23) lower end is stretched in tank body (1) inner chamber, make the second shell side channel connection tank body (1) inner chamber, and this housing (21) is provided with the vacuum orifice (13) with the first shell side channel connection.
2. a kind of vacuum receiver according to claim 1, it is characterized in that: described housing (21) is provided with a medium and goes out pipe (211) and be installed on medium to go out medium inlet pipe (212) in pipe (211) and mutually isolated, makes medium go out pipe (211) and forms tube-in-tube structure with medium inlet pipe (212); Wherein, medium inlet pipe (212) lower port respectively with the inlet communication of described first plate journey passage and the second plate journey passage, medium go out pipe (211) lower port respectively with the outlet of the first plate journey passage and the second plate journey passage.
3. a kind of vacuum receiver according to claim 2, it is characterized in that: between described the first heat exchange core (22) and the second heat exchange core (23), form stable assembling by forward and backward baffle plate (24,25) bar that is connected (26), wherein, interval is formed with between the first heat exchange core (22) and the second heat exchange core (23).
4. a kind of vacuum receiver according to claim 3, it is characterized in that: described forward and backward baffle plate (24,25) periphery is provided with the first spoiler (241) and the second spoiler (242), wherein, first spoiler (241) and the second spoiler (242) lay respectively at the first heat exchange core (22) and the second heat exchange core (23) is peripheral, and the second spoiler (242) is installed on the flange of tank body (1) upper end, the first spoiler (241) outer rim and housing (21) inwall are closely conflicted.
5. a kind of vacuum receiver according to claim 3, it is characterized in that: described front apron (24) is provided with respectively with first, second body (221,231) of the inlet communication of the first plate journey passage and the second plate journey passage, described medium inlet pipe (212) lower port is communicated with first, second body (221,231) by the first tube connector (213); Described backboard (25) is provided with respectively with the 3rd, the 4th body (222,232) of the outlet of the first plate journey passage and the second plate journey passage, described medium is gone out pipe (211) lower port and is communicated with by the second tube connector (214) and the 3rd, the 4th body (222,232).
6. a kind of vacuum receiver according to claim 5, is characterized in that: the internal diameter of described first, second, third, fourth body (221,231,222,232) is all consistent; First, second tube connector described (213,214) internal diameter size is twice of the first body (221) internal diameter size or more, and this first and second tube connector (213,214) end all has a reducing linkage section, and be connected with the second body (231) and the 4th body (232) respectively by this linkage section.
7. a kind of vacuum receiver according to claim 1-6 any one, it is characterized in that: described vacuum orifice (13) inside is also provided with one first cleaning mouthpiece (14), this the first cleaning mouthpiece (14) lower end is stretched in housing (21) inner chamber, and this first cleaning mouthpiece (14) lower end is provided with the first shower nozzle.
8. a kind of vacuum receiver according to claim 1-6 any one, it is characterized in that: described tank body (1) is provided with one second cleaning mouthpiece (15), this the second cleaning mouthpiece (15) end is stretched in the middle part of tank body (1) inner chamber, and this second cleaning mouthpiece (15) end is provided with the second shower nozzle.
9. a kind of vacuum receiver according to claim 1-6 any one, is characterized in that: the form (16) described tank body (1) being provided with at least one observable tank body (1) inner chamber situation.
10. a kind of vacuum receiver according to claim 1-6 any one, it is characterized in that: described tank body (1) is provided with capacitance liquid level meter interface (17), in this capacitance liquid level meter interface (17), capacitance liquid level meter is installed; Described tank body (1) lower end is provided with the feet (18) of at least three horizon adjustables.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410830758.8A CN104548670B (en) | 2014-12-25 | 2014-12-25 | A kind of vacuum receiver |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410830758.8A CN104548670B (en) | 2014-12-25 | 2014-12-25 | A kind of vacuum receiver |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104548670A true CN104548670A (en) | 2015-04-29 |
| CN104548670B CN104548670B (en) | 2016-05-11 |
Family
ID=53066393
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410830758.8A Active CN104548670B (en) | 2014-12-25 | 2014-12-25 | A kind of vacuum receiver |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104548670B (en) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201906485U (en) * | 2011-01-21 | 2011-07-27 | 淄博通达防腐设备有限公司 | Gas-liquid separation system |
| CN202802802U (en) * | 2012-10-08 | 2013-03-20 | 化大赛高（烟台）科技有限公司 | Dehydration and degassing primary fractionation device |
| WO2014118814A2 (en) * | 2013-01-30 | 2014-08-07 | Luigi Patron | Process with improved productivity for the conversion of heavy oils |
| CN203763913U (en) * | 2014-04-02 | 2014-08-13 | 上海南华换热器制造有限公司 | Degasser |
| CN204395533U (en) * | 2014-12-25 | 2015-06-17 | 东莞埃欧热能技术有限公司 | A kind of vacuum receiver |
-
2014
- 2014-12-25 CN CN201410830758.8A patent/CN104548670B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201906485U (en) * | 2011-01-21 | 2011-07-27 | 淄博通达防腐设备有限公司 | Gas-liquid separation system |
| CN202802802U (en) * | 2012-10-08 | 2013-03-20 | 化大赛高（烟台）科技有限公司 | Dehydration and degassing primary fractionation device |
| WO2014118814A2 (en) * | 2013-01-30 | 2014-08-07 | Luigi Patron | Process with improved productivity for the conversion of heavy oils |
| CN203763913U (en) * | 2014-04-02 | 2014-08-13 | 上海南华换热器制造有限公司 | Degasser |
| CN204395533U (en) * | 2014-12-25 | 2015-06-17 | 东莞埃欧热能技术有限公司 | A kind of vacuum receiver |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104548670B (en) | 2016-05-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203602597U (en) | Wine fermentation tank with aroma recovery device | |
| CN203663472U (en) | Efficient falling film evaporator | |
| CN204395533U (en) | A kind of vacuum receiver | |
| CN205227950U (en) | Oil separator and including this oil separator's condenser | |
| CN203132399U (en) | Clean tube type heat exchanger with double tube sheets | |
| CN104548670A (en) | Vacuum degassing tank | |
| CN204436899U (en) | A kind of open type oil tank for hydraulic system | |
| CN207532811U (en) | A kind of liquid heating evaporation enrichment facility | |
| CN205367783U (en) | Buck is with vertical cyclone film deaerating plant | |
| CN213628197U (en) | Spray absorption type vacuumizing unit | |
| CN204369596U (en) | Vacuum type deoxygenator | |
| CN210495296U (en) | Ethanol steam recovery device | |
| CN205925022U (en) | Traditional chinese medicine is concentrated jar | |
| CN109307259B (en) | Tower-free deaerator | |
| CN203458953U (en) | Spray absorption system with gas pumping unit | |
| CN106474757B (en) | The condenser and condensation method of steam forced circulation and vacuum energy-saving evaporator | |
| CN104075594A (en) | Double shell pass tubular heat exchanger | |
| CN104566333B (en) | A kind of Low Temperature Steam reclaimer | |
| CN203021522U (en) | Methane gas-liquid separating device | |
| CN204494680U (en) | Electrode humidifier nozzle component and unitary air handling unit | |
| CN213220962U (en) | Integrated forced circulation evaporation separator | |
| CN203861018U (en) | Instant heating type water dispenser | |
| CN204337811U (en) | The equipment complex of a kind of overhead condenser and return tank | |
| CN204436900U (en) | A kind of open type oil tank for hydraulic system | |
| CN103058301A (en) | Horizontal flash tank and low-temperature multi-effect distillation seawater desalination system |
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 |