CN101013003A - Hypergravity mass transfer apparatus - Google Patents
Hypergravity mass transfer apparatus Download PDFInfo
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- CN101013003A CN101013003A CN 200710067008 CN200710067008A CN101013003A CN 101013003 A CN101013003 A CN 101013003A CN 200710067008 CN200710067008 CN 200710067008 CN 200710067008 A CN200710067008 A CN 200710067008A CN 101013003 A CN101013003 A CN 101013003A
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- mass transfer
- transfer apparatus
- hypergravity
- shell
- gas
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- 238000012546 transfer Methods 0.000 title claims abstract description 29
- 239000007788 liquid Substances 0.000 claims abstract description 48
- 239000000835 fiber Substances 0.000 claims abstract description 10
- 239000012530 fluid Substances 0.000 claims description 9
- 238000009941 weaving Methods 0.000 claims description 6
- 230000002787 reinforcement Effects 0.000 claims description 4
- 238000005452 bending Methods 0.000 claims description 3
- 238000009792 diffusion process Methods 0.000 claims description 3
- 230000002093 peripheral effect Effects 0.000 claims description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 43
- 230000000694 effects Effects 0.000 description 8
- 238000005516 engineering process Methods 0.000 description 8
- 239000000126 substance Substances 0.000 description 7
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 5
- 239000003345 natural gas Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 150000005846 sugar alcohols Polymers 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000009938 salting Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 235000011132 calcium sulphate Nutrition 0.000 description 2
- 239000001175 calcium sulphate Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000007791 dehumidification Methods 0.000 description 2
- 239000002274 desiccant Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 150000004677 hydrates Chemical class 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000011069 regeneration method Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- -1 and chemistry Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- NMJORVOYSJLJGU-UHFFFAOYSA-N methane clathrate Chemical compound C.C.C.C.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O NMJORVOYSJLJGU-UHFFFAOYSA-N 0.000 description 1
- 239000003094 microcapsule Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000012782 phase change material Substances 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
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- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The invention discloses a hypergravity transfer unit, comprising a frame, a rotary axle and a liquid inlet tube. The frame is arranged with an air inlet, an air outlet and a liquid outlet. The rotary axle is arranged with a rotor which comprises a cylinder central axle, several coaxial plates parallel arranged on the outer wall of cylinder central axle, and several blades arranged on the cylinder central axles between the plates. The blades and the plates have spaces reducing radial from inner to outer. The liquid inlet tube is through the frame to reach the center of cylinder central axle. The air inlet is communicated with the inlet of cylinder central axle. The rotator is arranged arc plates and cylinder woven fiber layer. The invention can dry, cool, or heat air as well as pressurize the air. And the gas-liquid direction is clockwise, to reduce the resistance and reduce energy consumption.
Description
Technical field
The present invention relates to chemistry, chemical industry, environmental protection and refrigeration, air-conditioning, thermal power field, be specifically related to a kind of hypergravity mass transfer apparatus.
Background technology
Chemistry, chemical industry, environmental protection and air-conditioning, in the processes such as refrigeration, extensively exist and directly contact the heat and mass operation of carrying out between gas (vapour)-liquid, as absorbing sulfur in smoke with calcium sulphate soln in the wet desulphurization, utilize water and natural gas to prepare the accumulating that gas hydrates carry out natural gas in the gas industry, air-conditioning system often adopts spray chamber to handle air in textile industry, the technology that adopts moisture absorption liquid that air is dehumidified has then appearred in the comfort air conditioning system system in recent years, use polyalcohol, moisture absorption liquid such as salting liquid carry out desiccant dehumidification to air, the then available low grade residual heat thermal regeneration of weak solution after the dehumidifying, or the like.Present the most frequently used gas (vapour) liquid contact mass transfer equipment, as packed tower, board-like falling-film absorber etc. only rely on the weight-driven liquid film to flow, upgrade, and mass tranfer coefficient is lower, causes equipment volume huge.The basic principle of hypergravity mass transfer technology is to utilize unique flow behavior of multiphase flow system under the hypergravity condition, strengthen relative velocity between phase and phase and be in contact with one another, thereby realize mass-and heat-transfer process and chemical reaction process efficiently, the mode of obtaining hypergravity mainly is the formation centrifugal force field of turning by high speed rotating.The hypergravity mass transfer technology has obtained application in fields such as chemical industry, environmental protection at present; as " high-efficiency low-resistance concentric ring video disc filler revolving bed flow resistance and mass transfer characteristic research "; letter is abandoned non-, Deng Xianhe, Zhang Yajun; " sulfuric acid industry "; the 5th phase; the 11-15 page or leaf; 2000; and " high-gravity technology and the application in environmental protection thereof ", Zhao Xiaoxi, Deng Xianhe, Pan Chaoqun, Chen Haihui, " chemical industry environmental protection "; the 22nd the 3rd phase of volume; the 142-145 page or leaf, has been reported relevant research and progress in June, 2002.On October 19th, 2005, disclosed application number was a kind of super gravity liquid absorption dehumidifying and the regenerative system patent of invention of CN200510033125.5, it adopts the air processor of hypergravity mass transfer technology, utilize the mass transport process in the centrifugal force reinforcement air-treatment, used filler is board-like, wire mesh packing, hygroscopic solution is polyalcohol, salting liquid, operator scheme is adverse current, cross-flow, need overcome centrifugal force, has that air flow resistance is big, the shortcoming of function singleness.
Summary of the invention
Technical problem to be solved by this invention provides a kind of hypergravity mass transfer apparatus, in processing procedure, can realize supercharging to gas (vapour) body, reinforcement gas (vapour)-liquid contact absorbs, desorb, cooling, heating, processes such as synthetic, purification, reduce the device running resistance simultaneously, be convenient to gas (vapour) and flow, cut down the consumption of energy.
In order to solve the problems of the technologies described above, the technical solution used in the present invention is: a kind of hypergravity mass transfer apparatus, comprise shell, be located at rotating shaft and feed tube on the shell, shell is provided with air inlet, exhaust outlet and leakage fluid dram, described rotating shaft is provided with turns, turn and comprise the tubular central shaft, be located on the tubular central shaft outer wall the some coaxial plate that is parallel to each other and around the some blades on the tubular central shaft that is arranged between each parallel plate, blade and plate can play the supercharging of processed gas (vapour) body, enlarge the vapour-liquid contact area, produce hypergravity effects such as (centrifugal force); Be provided with the gap between described blade and plate, this gap radially from inside to outside reduces, and described feed tube passes shell and is in tubular central shaft center.Described blade bottom side also can directly be connected on the plate, establish radial groove and play the effect same at plate and blade joint, just change the gap position is set, the gap is arranged on plate and blade joint with the gap, certainly, described groove also can axially be provided with.
Above-mentioned blade is general to be adopted along equidistant optimizing structure of being provided with on the tubular central shaft circumferencial direction.
Described blade can be directly radially overhanging, but also forward direction or back are overhanging to bending, and described blade shape also can be the three-dimension curved surface shape, thereby increases contact-making surface area and supercharging area, improves pneumatic efficiency.
Preferably, described air inlet is communicated with the inlet of tubular central shaft, thereby makes airintake direction and feed liquor direction in the same way, and the resistance that is subjected in the time of can reducing the device operation like this cuts down the consumption of energy.
Improved, at described peripheral two ends and the fixed together stereo weaving tubular fibre structure that is connected of outer casing end inwall of also being provided with of turning, or the porous aggregate of other type, can enlarge the solution-air contact area on the one hand, also can bring into play the non-homogenous system centrifugation of gas (vapour)-liquid simultaneously.
Improved, also be provided with the arc plate of fixedlying connected in the described periphery of turning with outer casing inner wall, can form the diffusion bend between the arc plate, also can play effects such as enlarging solution-air contact area, the non-homogenous system separation of solution-air simultaneously.
Improved, be provided with the arc plate of fixedlying connected with outer casing inner wall in the described periphery of turning, position, arc plate outer edge is set up the fibre structure layer or the porous aggregate layer of body knitted cylindrical again, and the two together enlarges the solution-air contact area, realizes that the non-homogenous system of solution-air separates.
During work, gas (vapour) body enters from air inlet, liquid is sprayed between the coaxial plate and blade of turning from sparge pipe, equipment drives down rotation formation centrifugal force field at a high speed and turn externally, gas (vapour) body that enters is fully contacted with liquid absorb (as the dehumidifying of air), desorb (as the regeneration of weak solution), humidification, cooling (as directly handling air) or heating with chilled water, and chemistry, chemical industry synthetic (generating gas hydrates) etc. as water-natural gas, look liquid, gas (vapour) body kind and character and different, and then through the fibre structure layer of stereo weaving tubular, the passage exhaust outlet of compositions such as arc plate is discharged behind gas (vapour) separator, discharges through leakage fluid dram with the liquid that gas (vapour) body carries out after mass transfer contacts.
Device hypergravity mass transfer technology of the present invention, in the centrifugal force field that rotation forms at a high speed, make gas (vapour) body that enters (as air, natural gas, flue gas etc.) and liquid (as moisture absorption liquid, cold water, calcium sulphate soln etc.) fully contact, owing to be provided with blade between plate, make gas (vapour) body at desiccant dehumidification, synthetic or purification also is pressurized when absorbing, increased the mass transfer force in the processing procedure, and be provided with the arc plate of fixedlying connected and the fibre structure layer of stereo weaving tubular in the periphery of turning with outer casing inner wall, porous aggregate layer etc., further enlarged gas (vapour) liquid contact area, strengthened mass transfer, and played good gas (vapour) liquid separating effect, in addition owing to adopt concurrent, reduce gas (vapour) body flow resistance, reduced the resistance and the energy consumption of device operation.
Description of drawings
The invention will be further described below in conjunction with accompanying drawing:
Fig. 1 is the embodiment of the invention one structural representation;
Fig. 2 is the schematic diagram of blade construction among Fig. 1;
Fig. 3, Fig. 4 are the schematic diagram of other two kinds of structures of blade;
Fig. 5 is the embodiment of the invention two structural representations;
Fig. 6 is the portion that the turns cross sectional view among Fig. 5;
Fig. 7 is the embodiment of the invention three structural representations;
Fig. 8 is the portion that the turns cross sectional view among Fig. 7;
Fig. 9 is the embodiment of the invention four structural representations;
Figure 10 is the portion that the turns cross sectional view among Fig. 9;
Figure 11 is an I place structure for amplifying view among Fig. 1.
The specific embodiment
As Fig. 1, Figure 11, embodiment for hypergravity mass transfer apparatus of the present invention, comprise shell 1, be located at the rotating shaft 2 on the shell 1, feed tube 3, shell is provided with air inlet 11, exhaust outlet 12 and leakage fluid dram 13, leakage fluid dram 13 is located at shell 1 bottom, leakage fluid dram is the leakage fluid dram of band fluid-tight, prevent that gas from discharging from leakage fluid dram, be connected with in the described rotating shaft 2 and turn, turn and to form the hypergravity centrifugal force field in rotating shaft 2 high speed driven rotary, it comprises the tubular central shaft 41 that is connected with rotating shaft 2 ends, some blades 43 on the tubular central shaft 41 that is located at the some coaxial plate 42 that is parallel to each other on tubular central shaft 41 outer walls and is located at 42 of each parallel plates, tubular central shaft 41 can adopt axle construction identical in the prior art, as the tubular central shaft of grid type, guaranteeing that gas-liquid is smooth and easy passes through.Described blade 43 adopts along equidistant optimizing structure of being provided with on tubular central shaft 41 circumferencial directions, described plate 42 is the fillers as hypergravity mass transfer, first gas (vapour) liquid contact-making surface is provided, 42 of blade 43 and plates are provided with gap 5, this gap 5 radially from inside to outside reduces gradually, the mode that reduces in gap is preferably linear successively decreasing, and also can successively decrease for other curve form.Like this, blade and plate provide gas (vapour) the liquid contact-making surface of both sides on the one hand, on the one hand can be to processed air pressurized.In addition, also blade 43 directly can be connected with plate 42, plate 42 is suitably thickeied, and establishes radially or the axial groove of gradual change at plate 42 and blade joint, can play the effect in above-mentioned gap 5 equally.Be in tubular central shaft 41 centers of turning and pass shell 1 at blade 43 described feed tubes 3, described air inlet 11 is communicated with the inlet of tubular central shaft 41, thereby make airintake direction and feed liquor direction in the same way, the resistance that is subjected in the time of can reducing the device operation like this cuts down the consumption of energy.Be provided with whirlwind gas (vapour) separator 6 or silk screen gas (vapour) separator 7 at exhaust outlet 12 places, or both combinations, the drying of air is discharged in assurance.
Described blade 43 can be directly radially overhanging, as shown in Figure 3; Also but forward direction or back are overhanging to bending, as Fig. 2 and shown in Figure 4; Described blade shape also can be the three-dimension curved surface shape, with the pneumatic efficiency of raising gas boosting, and enlarges gas (vapour) liquid contact area and supercharging area, and three-dimension curved surface can be and centrifugal compressor blade similar structures.And enlarge gas (vapour) liquid contact area at the reinforcement groove that the sidewall of blade 43 also can be provided with different shape, play the non-homogenous system centrifugation of gas (vapour) liquid simultaneously.
Embodiment one is improved, as shown in Figure 5 and Figure 6, be embodiment two, can set up the fibre structure layer 9 of the stereo weaving tubular of fixedlying connected in the described periphery of turning with shell 1 inwall, can enlarge gas (vapour) liquid contact area on the one hand, play the non-homogenous system centrifugation of gas (vapour) liquid simultaneously, certainly, the fibre structure layer 9 of this stereo weaving tubular also can adopt packed bed formula structure or other similar structures to realize above-mentioned purpose.
Another kind to embodiment one improves, as shown in Figure 7 and Figure 8, be embodiment three, can set up the arc plate 8 of fixedlying connected in the described periphery of turning with shell 1 inwall, 8 of each arc plates can form the diffusion bend, can enlarge gas (vapour) liquid contact area on the one hand, also can play the effect that the non-homogenous system of gas (vapour) liquid separates simultaneously.
Embodiment two and embodiment three are combined, as Fig. 9 and shown in Figure 10, can obtain the preferred embodiment four of the present invention, be provided with the arc plate 8 of fixedlying connected with shell 1 inwall in the described periphery of turning, position, arc plate outer edge is set up the fibre structure layer 9 of body knitted cylindrical again, the two together enlarges gas (vapour) liquid contact area, realizes that the non-homogenous system of gas (vapour) liquid separates.
During work, gas enters from air inlet, liquid is sprayed between the coaxial plate and blade of turning from sparge pipe, equipment drives down rotation formation centrifugal force field at a high speed and turn externally, gas (vapour) body that enters is fully contacted with liquid, gas (vapour) body is in this or the dehumidifying that is dried, or be cooled, heat, or carry out chemical industry with liquid and synthesize, or be cleaned, look class of liquids and character and different, pass through the arc plate then behind gas (vapour) liquid/gas separator, to discharge, discharge through leakage fluid dram with the liquid that gas (vapour) body carries out after mass transfer contacts from exhaust outlet.This device can cool off gas (vapour) body, heating, and dehumidifying, humidification purifies, and the chemical reaction that also can carry out gas (vapour) body and liquid is used for chemical industry and synthesizes, as water-natural gas synthesis of natural gas hydrate or the like.According to concrete needs, the liquid that uses among the present invention can be low-temperature cold water, low temperature polyalcohol, organic or inorganic salting liquid, hot water, normal temperature polyalcohol etc.Described liquid can also adopt and contain the liquid that plays intensifying treatment effect effect solia particle in right amount, and described solia particle can be ice particulate, the phase-change material particle that is packaged into microcapsules and all kinds of catalyst particles etc.
Claims (10)
1, a kind of hypergravity mass transfer apparatus, comprise shell (1), be located at rotating shaft (2) and feed tube (3) on the shell (1), shell (1) is provided with air inlet (11), exhaust outlet (12) and leakage fluid dram (13), described rotating shaft (2) is provided with turns, the center of turning is provided with tubular central shaft (41), described feed tube (3) passes shell (1) and is in tubular central shaft (41) center, tubular central shaft outer wall is provided with some being parallel to each other and coaxial plate (42), it is characterized in that: be equipped with some blades (43) on the tubular central shaft between described each parallel plate (42), be provided with gap (5) between described blade (43) and plate (42), this gap (5) radially from inside to outside reduces.
2, according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: described blade (43) can be directly radially overhanging.
3, according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: described blade (43) but forward direction or the back overhanging to bending.
4, according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: be provided with the reinforcement groove at described blade (43) sidewall.
5, according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: described some blades (43) are along equidistantly being provided with on tubular central shaft (41) circumferencial direction.
6, according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: described air inlet (11) is communicated with the inlet of tubular central shaft (41).
7 according to the described a kind of hypergravity mass transfer apparatus of claim 1, it is characterized in that: locate to be provided with whirlwind gas-liquid separator (6) or silk screen gas-liquid separator (7) at exhaust outlet (12), or both combinations.
8, according to claim 1,5,6 or 7 described a kind of hypergravity mass transfer apparatus, it is characterized in that: peripheral fibre structure layer (9) or the filling batch that also is provided with the stereo weaving tubular of turning in described shell (1).
9, according to claim 1,5,6 or 7 described a kind of hypergravity mass transfer apparatus, it is characterized in that: be provided with the arc plate (8) of fixedlying connected in the described periphery of turning, form the diffusion bend between each arc plate (8) with shell (1) inwall.
10, according to claim 1,5,6 or 7 described a kind of hypergravity mass transfer apparatus, it is characterized in that: be provided with the arc plate (8) of fixedlying connected with shell (1) inwall in the described periphery of turning, the fibre structure layer (9) or the filling batch of body knitted cylindrical set up at arc plate (8) outer rim position again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200710067008XA CN100472165C (en) | 2007-01-30 | 2007-01-30 | Hypergravity mass transfer apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB200710067008XA CN100472165C (en) | 2007-01-30 | 2007-01-30 | Hypergravity mass transfer apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN101013003A true CN101013003A (en) | 2007-08-08 |
| CN100472165C CN100472165C (en) | 2009-03-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB200710067008XA Expired - Fee Related CN100472165C (en) | 2007-01-30 | 2007-01-30 | Hypergravity mass transfer apparatus |
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| CN (1) | CN100472165C (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104521599A (en) * | 2014-12-31 | 2015-04-22 | 山东中昊重工科技有限公司 | Supergravity air cooling equipment capable of removing natural dormancy of deciduous fruit trees |
| CN104567462A (en) * | 2014-12-31 | 2015-04-29 | 魏永阳 | Super-gravity heat exchange process |
| CN105080340A (en) * | 2015-09-20 | 2015-11-25 | 山西长林环保机械设备有限公司 | Clash centrifugal denitration process and equipment |
| CN108609678A (en) * | 2018-03-21 | 2018-10-02 | 国电菏泽发电有限公司 | The thermal wastewater concentrate fluidized crystallization drying system and method for hot-air pressure-cycling |
| CN110514027A (en) * | 2019-08-22 | 2019-11-29 | 东台宏仁气体有限公司 | A kind of rotary and telescopic nitrogen cooling device and its cooling means |
| CN111153552A (en) * | 2020-01-10 | 2020-05-15 | 重庆工业职业技术学院 | Breeding sewage treatment device |
| CN112337140A (en) * | 2019-08-09 | 2021-02-09 | 北京化工大学 | Method for removing volatile components in polymer by virtue of supergravity by supplementing heat energy in situ |
| CN112337139A (en) * | 2019-08-09 | 2021-02-09 | 北京化工大学 | In-situ heat-supplementing supergravity devolatilization device and application |
| CN113083179A (en) * | 2021-03-02 | 2021-07-09 | 北京化工大学 | Gas-liquid-solid three-phase supergravity reactor for coupling energy field and application |
| CN113877513A (en) * | 2021-11-15 | 2022-01-04 | 成都阿利特建材有限公司 | Hypergravity membrane reactor |
| CN114082391A (en) * | 2021-11-12 | 2022-02-25 | 武汉科技大学 | Self-stabilizing baffling type super-gravity rotating bed |
| CN114702090A (en) * | 2022-04-29 | 2022-07-05 | 南京航空航天大学 | Photovoltaic photo-thermal humidification and dehumidification system based on supergravity packed bed and working method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| TWI696489B (en) * | 2019-07-08 | 2020-06-21 | 超重力有限公司 | Exhaust gas treatment method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB757149A (en) * | 1953-06-29 | 1956-09-12 | Claes Wilhelm Pilo | Apparatus for the performance of an exchange of heat and/or soluble substances between two flowing media of different specific gravity |
| GB8305595D0 (en) * | 1983-03-01 | 1983-03-30 | Ici Plc | Evaporator |
-
2007
- 2007-01-30 CN CNB200710067008XA patent/CN100472165C/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104521599A (en) * | 2014-12-31 | 2015-04-22 | 山东中昊重工科技有限公司 | Supergravity air cooling equipment capable of removing natural dormancy of deciduous fruit trees |
| CN104567462A (en) * | 2014-12-31 | 2015-04-29 | 魏永阳 | Super-gravity heat exchange process |
| CN105080340A (en) * | 2015-09-20 | 2015-11-25 | 山西长林环保机械设备有限公司 | Clash centrifugal denitration process and equipment |
| CN108609678A (en) * | 2018-03-21 | 2018-10-02 | 国电菏泽发电有限公司 | The thermal wastewater concentrate fluidized crystallization drying system and method for hot-air pressure-cycling |
| CN108609678B (en) * | 2018-03-21 | 2024-02-06 | 国电菏泽发电有限公司 | Hot waste water concentrate fluidization crystallization drying system and method with hot air pressure swing circulation |
| CN112337139B (en) * | 2019-08-09 | 2022-04-19 | 北京化工大学 | In-situ heat-supplementing supergravity devolatilization device and application |
| CN112337140A (en) * | 2019-08-09 | 2021-02-09 | 北京化工大学 | Method for removing volatile components in polymer by virtue of supergravity by supplementing heat energy in situ |
| CN112337139A (en) * | 2019-08-09 | 2021-02-09 | 北京化工大学 | In-situ heat-supplementing supergravity devolatilization device and application |
| CN110514027B (en) * | 2019-08-22 | 2021-04-13 | 东台宏仁气体有限公司 | Rotary telescopic nitrogen cooling device and cooling method thereof |
| CN110514027A (en) * | 2019-08-22 | 2019-11-29 | 东台宏仁气体有限公司 | A kind of rotary and telescopic nitrogen cooling device and its cooling means |
| CN111153552B (en) * | 2020-01-10 | 2022-02-08 | 重庆工业职业技术学院 | Breeding sewage treatment device |
| CN111153552A (en) * | 2020-01-10 | 2020-05-15 | 重庆工业职业技术学院 | Breeding sewage treatment device |
| CN113083179A (en) * | 2021-03-02 | 2021-07-09 | 北京化工大学 | Gas-liquid-solid three-phase supergravity reactor for coupling energy field and application |
| CN114082391A (en) * | 2021-11-12 | 2022-02-25 | 武汉科技大学 | Self-stabilizing baffling type super-gravity rotating bed |
| CN113877513A (en) * | 2021-11-15 | 2022-01-04 | 成都阿利特建材有限公司 | Hypergravity membrane reactor |
| CN114702090A (en) * | 2022-04-29 | 2022-07-05 | 南京航空航天大学 | Photovoltaic photo-thermal humidification and dehumidification system based on supergravity packed bed and working method thereof |
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| Publication number | Publication date |
|---|---|
| CN100472165C (en) | 2009-03-25 |
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