CN104399268B - Prepare the upper cover of concentrate - Google Patents
Prepare the upper cover of concentrate Download PDFInfo
- Publication number
- CN104399268B CN104399268B CN201410706695.5A CN201410706695A CN104399268B CN 104399268 B CN104399268 B CN 104399268B CN 201410706695 A CN201410706695 A CN 201410706695A CN 104399268 B CN104399268 B CN 104399268B
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- China
- Prior art keywords
- lid
- upper cover
- inclined plane
- strip
- close
- Prior art date
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- Heat-Pump Type And Storage Water Heaters (AREA)
Abstract
The present invention relates to concentrate preparation field, particular but not exclusively relate to a kind of upper cover preparing concentrate, it has lid, it is characterized in that upper cover is provided with condensing unit, the collection unit of condensing unit is positioned at the inside of upper cover, collection unit comprises the strip being close to crown in lid and converges bar, is close to the collector ring of lid inner peripheral surface, the opening of collector ring is towards the top of lid, collector ring and lid form chamber of confluxing, the end that strip converges bar extends to chamber of confluxing, and chamber of confluxing is in communication with the outside by output channel; The cooling end of condensing unit is positioned at the outside of upper cover, cooling end comprises the annular wafer of multiple coaxial setting, annular wafer is arranged along the crown of lid, the axis of annular wafer and the axis coaxle of lid are arranged, the outer crown of lid is close in the bottom of annular wafer, apical ring is provided with inlet channel, and base ring is provided with outlet conduit.Upper cover condensation efficiency disclosed by the invention is high.
Description
Technical field
The present invention relates to concentrate preparation field, particular but not exclusively relate to a kind of upper cover preparing concentrate.
Background technology
The boiling point of water reduces along with the reduction of air pressure, therefore reducing pressure can make water seethe with excitement at relatively low temperatures, the water of boiling constantly makes liquid water transitions be hot water and steam, the water vapour of heat can be condensed into water smoke at cold and hot interface place, a large amount of water smoke pools water droplet, and a large amount of water droplets accumulates current.
For this reason, there has been proposed and a kind ofly utilize above-mentioned principle by the device of the moisture removal in mixed liquor, namely prepare the equipment of concentrate, the vapours produced in boiler is condensed into aqueous water, again water is transported in special container, thus the moisture in mixed liquor is reduced, realize concentrated effect.
How effectively the vapours in boiler to be condensed into aqueous water.
Summary of the invention
The object of the invention is to solve the problem, and provide a kind of low pressure low boiling to prepare the upper cover of concentrate equipment.
For this reason, the invention provides a kind of upper cover preparing concentrate, it comprises lid, it is characterized in that described upper cover is provided with condensing unit, the collection unit of condensing unit is positioned at the inside of upper cover, and collection unit comprises the strip being close to crown in lid and converges bar, is close to the collector ring of lid inner peripheral surface, the opening of collector ring is towards the top of lid, collector ring and lid form chamber of confluxing, and the end that strip converges bar extends to chamber of confluxing, and chamber of confluxing is in communication with the outside by output channel.The cooling end of condensing unit is positioned at the outside of upper cover, cooling end comprises the annular wafer of multiple coaxial setting, annular wafer is arranged along the crown of lid, the axis of annular wafer and the axis coaxle of lid are arranged, the outer crown of lid is close in the bottom of annular wafer, apical ring is provided with inlet channel, and base ring is provided with outlet conduit.
Particularly, strip converges bar and is provided with the binding face corresponding to crown in lid, two sides perpendicular to binding face are symmetrically arranged with the first arc surface of phase concave, the end face being parallel to binding face is provided with the second arc surface of indent, spill proof edge is formed between first arc surface and the second arc surface, strip converges bar and is provided with the first inclined plane and the second inclined plane near top, first inclined plane and the second inclined plane angle are obtuse angle, second inclined plane more converges to strip that the top of bar is close more to tilt to binding face, more to converging, the top of bar is close more to tilt to binding face first inclined plane, second arc surface extends to the second inclined plane, first arc surface extends to the first inclined plane.
Again particularly, the monolateral cross section of collector ring is " L " shape, and the base vertical of " L " is in the inner peripheral surface of upper cover, and the stile of " L " is parallel to the inner peripheral surface of upper cover.
Again particularly, the inner spout of described output channel is near the top of the conflux bottom in chamber and the stile far below " L ", and the bottom of described inlet channel is fixedly connected with the top of lid, and the bottom of inlet channel is provided with multiple delivery port.
Again particularly, the top of described annular wafer reduces to the distance of the bottom surface of lid with the increase of diameter itself.
Beneficial effect
The multiple coaxial setting of boiler upper cover and in ladder the cooling end of the condensing unit that the annular wafer of dress is formed, add the contact surface of boiler upper cover and cooling fluid, improve the cooling effectiveness of cooling fluid.
Strip converges the first arc surface and second arc surface of bar setting, adds cold and hot interface, improves the condensation efficiency of vapours.
Strip converges the spill proof edge of bar setting by the surface tension effects of liquid, condensed drop is slipped to along the first arc surface and the second arc surface and confluxes in chamber, avoid condensed drop and directly drop onto in concentrate, cause thickening efficiency to reduce.
When the moment that second switch and the 3rd switch are unlocked, the water in pipeline will be pushed back in boiler, due to the cushioning effect in chamber of confluxing, water be rested on and confluxes in chamber, instead of directly enter in concentrate.
Accompanying drawing explanation
Reference accompanying drawing is in the explanation of the embodiment provided as non-limiting example below, and the present invention and superiority thereof will be better understood, and accompanying drawing is as follows:
Fig. 1 is the stereogram preparing concentrate equipment disclosed by the invention;
Fig. 2 is the stereogram of the boiler in Fig. 1;
Fig. 3 is the exploded perspective view of boiler in Fig. 2;
Fig. 4 is the stereogram after boiler in Fig. 3 removes upper cover;
Fig. 5 is the top view of the upper cover of boiler in Fig. 3;
Fig. 6 is the stereogram of the upper cover in Fig. 5;
Fig. 7 is the stereogram at another visual angle of upper cover in Fig. 5;
Fig. 8 is the exploded perspective view of the upper cover in Fig. 5;
Fig. 9 is the sectional view along A-A direction in Fig. 5;
Figure 10 is the sectional view along B-B direction in Fig. 5;
Figure 11 is the partial enlarged drawing at I place in Figure 12;
Figure 12 is the stereogram of the single strip convergence bar in Fig. 8;
Figure 13 is the partial enlarged drawing at II place in Figure 12;
Figure 14 is the fragmentary perspective cross sectional view storing stream unit in Fig. 1;
Figure 15 is the enlarged top portion isometric figure storing stream unit in Figure 14;
The exploded perspective view of the second switch in Figure 16 Figure 15 and the 3rd switch;
Description of reference numerals
1. boiler unit; 11. upper covers; 12. heating units; 13. sidewalls; 14. sampling units; 15. charging apertures; 16. discharging openings; 1101. lid; 1102. collector ring; 1103. strips converge bar; 1104. annular wafer; 1105. output channel; 1106. inlet channel; 1107. outlet conduit; 1108. admission line; 1109. delivery port; 1103a. binding face; 1103b. the first arc surface; 1103c. the second arc surface; 1103d. spill proof edge; 1103e. the second inclined plane; 1103f. the first inclined plane; 1103g. the 3rd inclined plane; 2. store stream unit; 20. coupling blocks; 21. cylindrical shells; 22. the 4th switches; 23. the 3rd switches;
24. second switches; 25. first switches; 26. water level mark pipes; 27. the 4th pipelines; 28. the 3rd pipelines; 29. second pipes; 210. first pipelines; 201. circular shaft; 3. cooling unit; 4. decompressing unit.
Detailed description of the invention
In order to distinguish the inner spout of component and the outer mouth of pipe, port pipeline being positioned at container is called inner spout, and the port be positioned at by pipeline outside container is called the outer mouth of pipe.
As shown in Figure 1, the equipment preparing concentrate disclosed by the invention, it comprises boiler unit 1, store stream unit 2, cooling unit 3, decompressing unit 4, the output channel 1105 in the chamber of confluxing of boiler unit 1 with store the second switch 24 flowing unit 2 and connect, the outlet conduit 1107 of the cooling end of boiler unit 1 is connected by the input of switch with cooling unit 3, the inlet channel 1106 of the cooling end of boiler unit 1 is connected by the output of switch with cooling unit 3, the 3rd switch 23 storing stream unit 2 is connected by the input of pipeline with decompressing unit 4, the first switch 25 and the 4th switch 22 that store stream unit 2 connect with air.
As in Figure 2-4, the sidewall 13 of boiler unit 1 is provided with sampling unit 14 near bottom place, the upper cover 11 of boiler unit 1 is provided with condensing unit, and boiler unit 1 has airtight structure, and its inner bottom part is provided with charging aperture 15, discharging opening 16 and heating unit 12.
As Fig. 5, 6, 9, shown in 10, the cooling end of condensing unit is positioned at the outside of upper cover 11, cooling end comprises the annular wafer 1104 of multiple coaxial setting, annular wafer 1104 is arranged along the crown of lid 1101, the axis of annular wafer 1104 and the axis coaxle of lid 1101 are arranged, the outer crown of lid 1101 is close in the bottom of annular wafer 1104, the top of annular wafer 1104 reduces to the distance of the bottom surface of lid 1101 with the increase of diameter itself, apical ring is provided with inlet channel 1106, the bottom of inlet channel 1106 is fixedly connected with the top of lid 1101, the bottom of inlet channel 1106 is provided with multiple delivery port 1109, base ring is provided with outlet conduit 1107, water at low temperature flows to apical ring by inlet channel 1106, apical ring overflows after being full of water at low temperature to next ring, water at low temperature sequentially overflows each ring, finally discharge from the outlet conduit 1107 of base ring, obviously, the water temperature of apical ring is lower than the water temperature of base ring.
As Fig. 7, 8, 9, shown in 10, the collection unit of condensing unit is positioned at the inside of upper cover 11, collection unit comprises the strip being close to crown in lid 1101 and converges bar 1103, be close to the collector ring 1102 of lid 1101 inner peripheral surface, the opening of collector ring 1102 is towards the top of lid 1101, collector ring 1102 and lid 1101 form chamber of confluxing, the end that strip converges bar 1103 extends to chamber of confluxing, the monolateral cross section of collector ring 1102 is " L " shape, the base vertical of " L " is in the inner peripheral surface of upper cover 11, the stile of " L " is parallel to the inner peripheral surface of upper cover 11, chamber of confluxing is in communication with the outside by output channel 1105, the inner spout of output channel 1105 is near the top of the conflux bottom in chamber and the stile far below " L ".
As Figure 11, 12, shown in 13, strip converges bar 1103 and is provided with the binding face 1103a corresponding to crown in lid 1101, two sides perpendicular to binding face 1103a are symmetrically arranged with the first arc surface 1103b of phase concave, the end face being parallel to binding face 1103a is provided with the second arc surface 1103c of indent, spill proof edge 1103d is formed between first arc surface 1103b and the second arc surface 1103c, strip converges bar 1103 and is provided with the first inclined plane 1103f and the second inclined plane 1103e near top, first inclined plane 1103f and the second inclined plane 1103e angle are obtuse angle, second inclined plane 1103e more converges to strip that the top of bar 1103 is close more to tilt to binding face 1103a, more to converging, the top of bar is close more to tilt to binding face 1103a first inclined plane 1103f, second arc surface 1103c extends to the second inclined plane 1103e, first arc surface 1103b extends to the first inclined plane 1103f.Strip converges bar 1103 and is symmetrically arranged with the 3rd inclined plane 1103g near the first inclined plane 1103f end, strip is converged bar 1103 and is configured to a wedge angle near the first beveled end by the 3rd inclined plane 1103g, and multiple strip converges bar 1103 and matches with face the mode be close to by the 3rd inclined plane 1103g and evenly form a circle around wedge angle.
After the first arc surface 1103b that the strip that vapours in boiler encounters low temperature converges bar 1103 or the second arc surface 1103c, be condensed into drop, under the synergy of spill proof edge 1103d and Surface Tension of Liquid Drops, drop converges the first arc surface 1103b of bar 1103 or the second arc surface 1103c along strip and is slipped to and confluxes in chamber, discharges chamber of confluxing after the drop confluxed in chamber collects by output channel 1105.
As Figure 14, shown in 15, store the cylindrical shell 21 that stream unit 2 comprises sealing, first pipeline 210, second pipe 29, 3rd pipeline 28, 4th pipeline 27, first switch 25, second switch 24, 3rd switch 23, 4th switch 22 and water level mark pipe 26, cylindrical shell 21 is by the first pipeline 210, second pipe 29, 3rd pipeline 28, 4th pipeline 27 and the external world communicate, first pipeline 210, second pipe 29, 3rd pipeline 28, 4th pipeline 27 is respectively by the first switch 25, second switch 24, 3rd switch 23, 4th switch 22 realizes opening and closing, first pipeline 210 is positioned at cylindrical shell 21 near bottom place, the inner spout of second pipe 29 is near the bottom of cylindrical shell 21 but higher than the inner spout of the first pipeline 210, the inner spout of the 3rd pipeline 28 and the inner spout of the 4th pipeline 27 are near the top of cylindrical shell 21.
As shown in figure 16, second switch 24 and the 3rd switch 23 synchronization action, both are realized by following structure by synchronization action, there is the coupling block 20 with switch knob respective profile, at its head and the tail two ends, respectively through hole is set, simultaneously also through hole is set in the relevant position of switch knob, between handle coupling block 20 being arranged on two switches, by two circular shafts 201, handle and coupling block 20 are connected, then by back-up ring, circular shaft 201, handle, coupling block 20 three are fixed.
The equipment preparing concentrate disclosed by the invention comprises decompression process, condensation process, stores and flow through journey, drainage procedure.
Decompression process: close the first switch 25, the 4th switch 22 and the 6th switch, opens second switch 24, the 3rd switch 23, the 5th switch, the 7th switch, the 8th switch and the 9th switch.Open decompressing unit 4, make the gas in boiler enter decompressing unit 4 by the 5th switch, second switch 24, the 3rd switch 23, the 9th switch successively, from but air pressure in boiler reduce.
Condensation process: open cooling unit 3, the cooling fluid of cooling unit 3 is circulated by the 7th switch, apical ring, base ring and the 8th switch successively, makes the temperature of boiler top cover lower than the temperature of vapours in boiler by cooling fluid.
Open the heating unit 12 in boiler, the temperature of liquid to be concentrated in boiler is improved, because low pressure in boiler makes the boiling point of the moisture in solution to be concentrated also reduce, so make the water in solution to be concentrated seethe with excitement at a lower temperature, and then produce the water vapour of heat, the water vapour of heat is encountered the rear condensation of strip convergence bar 1103 of boiler upper cover 11 relative low temperature and is gathered into water droplet, under the synergy of spill proof edge 1103d and water drops surface tension force, water droplet converges the first arc surface 1103b of bar 1103 or the second arc surface 1103c along strip and is slipped to and confluxes in chamber, conflux to summarize in chamber and converge from strip the water that bar 1103 landing gets off.By condensation process, the moisture in the solution to be concentrated in boiler is constantly transferred to and confluxes in chamber, and then moisture in solution to be concentrated is reduced.
Store and flow through journey: after the water level confluxed in chamber exceedes the inner spout of output channel 1105, the water confluxed in chamber is discharged to by output channel 1105 and stores in stream unit 2, successively by the 5th switch, second switch 24, store to flow through in journey and there will be following three kinds of situations: 1. the air pressure in boiler is greater than the air pressure stored in stream unit 2,2. the air pressure in boiler equals to store the air pressure in stream unit 2, and the air pressure 3. in boiler is lower than the air pressure stored in stream unit 2.
During the situation 1 of being in, the water confluxed in chamber stores stream unit 2 from being pressed under the influence of air pressure; During the situation 2 of being in, because chamber of confluxing is higher than storing stream unit 2, so the water confluxed in chamber flows under gravity store stream unit 2; During the situation 3 of being in, open decompressing unit 4, the air pressure stored in stream unit 2 is reduced, and lower than the air pressure in boiler, makes situation 3 become situation 1 or 2; Store stream unit 2 by above three kinds of mode retainings.
Due to heating unit 12 continuous heating in boiler, so the temperature in boiler is higher than the temperature stored in stream unit 2, namely cause the air pressure in boiler higher than the air pressure stored in stream unit 2, therefore heating can impel the appearance of situation 1.
After the concentrate in boiler reaches predetermined concentration, heating unit 12 stops heating, air pressure in boiler declines, in order to avoid occurring that air pressure in boiler is lower than the air pressure stored in stream unit 2, decompressing unit 4 is needed to start, making to store air pressure in stream unit 2 lower than the air pressure in boiler by decompressing unit 4, entering to store stream unit 2 by remaining the condensed hydraulic pressure of water vapour in boiler.Because the water level confluxed in chamber is higher than output channel 1105 inner spout, so the water vapour in boiler can not directly enter store stream unit 2, thus reduce the harmful effect of water vapour to decompressing unit 4, inner spout due to second pipe 29 is positioned at the bottom place near cylindrical shell 21, and the inner spout of the 3rd pipeline 28 is near the top place of cylindrical shell 21, so when decompressing unit 4 works, avoid water and be immediately inhaled into the 3rd pipeline 28 after second pipe 29 is forced out, the top water that can reduce in cylindrical shell 21 that the inner spout of the 3rd pipeline 28 is arranged in cylindrical shell 21 enters the risk of the 3rd pipeline 28.
Drainage procedure: after the water level mark pipe 26 display water level stored in stream unit 2 reaches predetermined value, first close second switch 24, because second switch 24 and the 3rd switch 23 are by coupling block 20 synchronous interaction, so, while closing second switch 24, the 3rd switch 23 is also closed, after this, the water of condensation in boiler is by the chamber temporary reservoir that confluxes, after second switch 24 and the 3rd switch 23 are closed, store stream unit 2 to keep apart with boiler, open the 4th switch 22, make to store the air pressure flowed in unit 2 equal with extraneous atmospheric pressure, after air pressure balance, open the first switch 25, due to the effect of gravity, the water stored in stream unit 2 flows out from the first switch 25, realize the draining storing stream unit 2.After storing the water in stream unit 2 and be drained, first close the first switch 25 and the 4th switch 22, make to store stream unit 2 and isolated from atmosphere, open second switch 24 again, 3rd switch 23 is also unlocked simultaneously, due to store stream unit 2 in air pressure higher than the air pressure in boiler, so the moment that second switch 24 and the 3rd switch 23 are unlocked, water in pipeline will be pushed back in boiler, due to the cushioning effect in chamber of confluxing, water is rested on and confluxes in chamber, instead of directly enter in concentrate, after the air pressure stored in stream unit 2 and the air pressure balance in boiler, the condensed water of buffer memory in chamber that confluxes flows under gravity and stores stream unit 2, in order to maintain the environment under low pressure in boiler, need to open decompressing unit 4, the air pressure in boiler is made to maintain predetermined value, decompressing unit 4 open after can accelerate the water confluxed in chamber enter store stream unit 2.
After concentrate in boiler reaches predetermined concentration, first close heating unit 12, decompressing unit 4, the 5th switch, open the 6th switch again, extraneous gas enters boiler internal by admission line 1108, makes the air pressure in boiler and ambient atmosphere pressure balanced, air pressure in boiler raises than time concentrated, the boiling point of the water in concentrate also increases, because heating unit 12 is closed, so the water in concentrate stops boiling, concentrate no longer loses moisture, and namely concentrate keeps existing concentration.Open discharging opening 16, the concentrate prepared is flowed out by discharging opening 16, after concentrate is drained, close discharging opening 16, open charging aperture 15, make liquid to be concentrated enter boiler by charging aperture 15, after liquid to be concentrated reaches scheduled volume, close charging aperture 15 and the 6th switch, boiler and ambient atmosphere are isolated, enters next concentration flow path.
Obviously, can solution to be concentrated be inputted at boiler or while exporting concentrate, the water stored in stream unit 2 be discharged.Detailed process is: first close the 9th switch, open the 6th switch, due to draught head, the water confluxed in chamber is pressed into and stores stream unit 2, until boiler, store stream both unit 2 in air pressure and atmospheric pressure balance after, the water confluxed in chamber flows under gravity and stores stream unit 2, opens the first switch 25 simultaneously, and the water stored in stream unit 2 is discharged.
Decompressing unit 4 is aspiration pump or vavuum pump.Cooling unit 3 is provided with input and output, cooling fluid enters cooling unit 3 from input, the heat of cooling fluid is dispersed in air by the fin by cooling unit 3, and then makes the temperature of cooling fluid of cooling unit 3 output lower than the temperature of the cooling fluid of input.
Claims (3)
1. prepare the upper cover (11) of concentrate for one kind, it has lid (1101), it is characterized in that, upper cover (11) is provided with condensing unit, the collection unit of condensing unit is positioned at the inside of upper cover (11), collection unit comprises the strip being close to lid (1101) interior crown and converges bar (1103), be close to the collector ring (1102) of lid (1101) inner peripheral surface, the opening of collector ring (1102) is towards the top of lid (1101), collector ring (1102) and lid (1101) form chamber of confluxing, the end that strip converges bar (1103) extends to chamber of confluxing, chamber of confluxing is in communication with the outside by output channel (1105), the cooling end of condensing unit is positioned at the outside of upper cover (11), cooling end comprises the annular wafer (1104) of multiple coaxial setting, annular wafer (1104) is arranged along the crown of lid (1101), the axis of annular wafer (1104) and the axis coaxle of lid (1101) are arranged, the outer crown of lid (1101) is close in the bottom of annular wafer (1104), apical ring is provided with inlet channel (1106), and base ring is provided with outlet conduit (1107), described strip converges bar (1103) and is provided with the corresponding binding face of interior crown (1103a) with lid (1101), two sides perpendicular to binding face (1103a) are symmetrically arranged with first arc surface (1103b) of phase concave, the end face being parallel to binding face (1103a) is provided with second arc surface (1103c) of indent, spill proof edge (1103d) is formed between first arc surface (1103b) and the second arc surface (1103c), strip converges bar (1103) and top is provided with the first inclined plane (1103f) and the second inclined plane (1103e), first inclined plane (1103f) and the second inclined plane (1103e) angle are obtuse angle, second inclined plane (1103e) more converges to strip that the top of bar (1103) is close more to tilt to binding face (1103a), more to converging, the top of bar is close more to tilt to binding face (1103a) first inclined plane (1103f), second arc surface (1103c) extends to the second inclined plane (1103e), first arc surface (1103b) extends to the first inclined plane (1103f), strip converges bar (1103) and is symmetrically arranged with the 3rd inclined plane (1103g) near the first inclined plane (1103f) end, strip is converged bar (1103) and is configured to a wedge angle near the first beveled end by the 3rd inclined plane (1103g), multiple strip converges bar (1103) and matches with face the mode be close to by the 3rd inclined plane (1103g) and evenly form a circle around wedge angle.
2. a kind of upper cover (11) preparing concentrate according to claim 1, it is characterized in that the monolateral cross section of described collector ring (1102) is for " L " shape, the base vertical of " L " is in the inner peripheral surface of upper cover (11), and the stile of " L " is parallel to the inner peripheral surface of upper cover (11).
3. a kind of upper cover (11) preparing concentrate according to claim 1, is characterized in that the top of described annular wafer (1104) reduces to the distance of the bottom surface of lid (1101) with the increase of diameter itself.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410706695.5A CN104399268B (en) | 2014-11-28 | 2014-11-28 | Prepare the upper cover of concentrate |
| AU2015100483A AU2015100483A4 (en) | 2014-11-28 | 2015-04-14 | Upper cover for concentrates preparation device |
| AU2015100484A AU2015100484A4 (en) | 2014-11-28 | 2015-04-14 | Design method for upper cover for concentrates preparation device |
| IES20150246A IES86725B2 (en) | 2014-11-28 | 2015-08-11 | Upper cover for concentrates preparation device |
| IE20150234A IE20150234A1 (en) | 2014-11-28 | 2015-08-11 | Upper cover for concentrates preparation device |
| GBGB1520941.4A GB201520941D0 (en) | 2014-11-28 | 2015-11-27 | Upper cover for concentrates preparation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410706695.5A CN104399268B (en) | 2014-11-28 | 2014-11-28 | Prepare the upper cover of concentrate |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104399268A CN104399268A (en) | 2015-03-11 |
| CN104399268B true CN104399268B (en) | 2015-12-30 |
Family
ID=52636972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410706695.5A Expired - Fee Related CN104399268B (en) | 2014-11-28 | 2014-11-28 | Prepare the upper cover of concentrate |
Country Status (4)
| Country | Link |
|---|---|
| CN (1) | CN104399268B (en) |
| AU (2) | AU2015100484A4 (en) |
| GB (1) | GB201520941D0 (en) |
| IE (2) | IES86725B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104990426A (en) * | 2015-06-04 | 2015-10-21 | 江苏进源压力容器有限公司 | High-efficiency energy-saving evaporative condenser |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1998047595A1 (en) * | 1997-04-24 | 1998-10-29 | T.I.B. S.N.C. | A separator device for removing pollutants from waste water |
| JP2006175378A (en) * | 2004-12-24 | 2006-07-06 | Nisso Engineering Co Ltd | Evaporation device of foamable solution and its evaporation method |
| CN101314083A (en) * | 2007-05-28 | 2008-12-03 | 株式会社日立工业设备技术 | Liquid condensation system |
| CN101444676A (en) * | 2007-11-27 | 2009-06-03 | 贵阳铝镁设计研究院 | Water vapor baffling reclamation plant |
| CN101836935A (en) * | 2010-01-14 | 2010-09-22 | 徐自升 | Common-pressure herb-decocting machine with internal vacuum condensing device and condensing cover |
| CN202666438U (en) * | 2012-06-18 | 2013-01-16 | 博特瑞姆斯化工技术（北京）有限公司 | Countercurrent falling-film concentrating unit |
| CN204233795U (en) * | 2014-11-28 | 2015-04-01 | 厦门艾卓工业设计有限公司 | Prepare the upper cover of concentrate |
-
2014
- 2014-11-28 CN CN201410706695.5A patent/CN104399268B/en not_active Expired - Fee Related
-
2015
- 2015-04-14 AU AU2015100484A patent/AU2015100484A4/en not_active Ceased
- 2015-04-14 AU AU2015100483A patent/AU2015100483A4/en not_active Ceased
- 2015-08-11 IE IES20150246A patent/IES86725B2/en not_active IP Right Cessation
- 2015-08-11 IE IE20150234A patent/IE20150234A1/en not_active Application Discontinuation
- 2015-11-27 GB GBGB1520941.4A patent/GB201520941D0/en not_active Ceased
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO1998047595A1 (en) * | 1997-04-24 | 1998-10-29 | T.I.B. S.N.C. | A separator device for removing pollutants from waste water |
| JP2006175378A (en) * | 2004-12-24 | 2006-07-06 | Nisso Engineering Co Ltd | Evaporation device of foamable solution and its evaporation method |
| CN101314083A (en) * | 2007-05-28 | 2008-12-03 | 株式会社日立工业设备技术 | Liquid condensation system |
| CN101444676A (en) * | 2007-11-27 | 2009-06-03 | 贵阳铝镁设计研究院 | Water vapor baffling reclamation plant |
| CN101836935A (en) * | 2010-01-14 | 2010-09-22 | 徐自升 | Common-pressure herb-decocting machine with internal vacuum condensing device and condensing cover |
| CN202666438U (en) * | 2012-06-18 | 2013-01-16 | 博特瑞姆斯化工技术（北京）有限公司 | Countercurrent falling-film concentrating unit |
| CN204233795U (en) * | 2014-11-28 | 2015-04-01 | 厦门艾卓工业设计有限公司 | Prepare the upper cover of concentrate |
Also Published As
| Publication number | Publication date |
|---|---|
| IES20150246A2 (en) | 2016-06-01 |
| GB201520941D0 (en) | 2016-01-13 |
| CN104399268A (en) | 2015-03-11 |
| AU2015100484A4 (en) | 2015-05-21 |
| AU2015100483A4 (en) | 2015-05-21 |
| IES86725B2 (en) | 2016-11-16 |
| IE20150234A1 (en) | 2016-06-01 |
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