CN1306996C - A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof - Google Patents
A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof Download PDFInfo
- Publication number
- CN1306996C CN1306996C CNB2004100140234A CN200410014023A CN1306996C CN 1306996 C CN1306996 C CN 1306996C CN B2004100140234 A CNB2004100140234 A CN B2004100140234A CN 200410014023 A CN200410014023 A CN 200410014023A CN 1306996 C CN1306996 C CN 1306996C
- Authority
- CN
- China
- Prior art keywords
- adsorbent
- adsorption material
- foamed aluminum
- salt
- diameter
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Porous Artificial Stone Or Porous Ceramic Products (AREA)
Abstract
The present invention relates to an adsorbent / foamed aluminum compound adsorption material and a preparation method thereof, which is characterized by filling spherical zeolite or molecular sieve particles with a diameter of 3 to 6mm into a mold to 20 to 60mm in height, adding table salt particles with a diameter of less than 1mm according to the volume ratio of table salt to an adsorbent granule stack of 4:6, and uniformly filling; pressurizing, tightly prepressing, and preheating to 500 to 600 DEG C; pouring the molten aluminum into the mold according to the volume ratio of the molten aluminum to the adsorbent granule stack of 2:8, and pressurizing to 2 to 5 atm; washing to dissolute and extract salt after cooling solidification, and keeping a constant temperature of 350 DEG C for 3 hours. The prepared adsorbent/ foamed aluminum compound adsorption material with the thermal coefficient of 1 to 4 W/m. K is formed by that clearance among particles accounting for 60 to 65% of the total volume is filled with the through hole foamed aluminum accounting for 10% to 25% of the total volume; the prepared adsorbent/ foamed aluminum compound adsorption material can also form a through hole foamed aluminum structure with scarcely affected mass transfer performance and high structural strength and obviously improve the heat transfer performance of adsorbent beds.
Description
Technical field:
The invention belongs to the absorption type refrigerating sorbing material, particularly adsorbent/foamed aluminium composite adsorbing material and preparation method thereof.
Background technology:
Zeolite and molecular sieve are sorbing material commonly used in the absorption type refrigerating, are porous media material, and heat-conductive characteristic is low, is 0.08~0.1W/mK as the stacking bed thermal conductivity factor of zeolite granular, and this just makes, and refrigeration system is adsorbed, the desorption cycle is long, and efficient is low." the solid adsorption refrigeration meeting " held at Paris, FRA in November, 1992 (Solid Sorption Refrigeration Sym., Paris, France, 1992, Nov.:44-52) mentioned a kind of directly method of doping aluminium powder and iron powder in absorbent particles in the paper, but this method is difficult to make these high thermal conductivity coefficient materials to form continuous phase, so the effective thermal conductivity raising is not obvious.Britain's academic journal " heat recovery system and cogeneration " (Heat Recovery System ﹠amp; CHP, 1993, once proposed 13:297-300) metal foam that the copper or the nickel foil bonding of zeolite molecular sieve and plot ratio 35% are made is evenly mixed, with organic binder cemented, compression was under high pressure dried 3 hours under 1000 ℃ of high temperature then, activated at last, can significantly improve thermal conductivity factor, but this method can cause simultaneously mass tranfer coefficient significantly to reduce and complex process.A kind of " lump zeolite adsorbent with excellent heat conductivity and absorption property " that Chinese invention patent CN 1266741A proposes is compound zeolite powder and waterglass, and thermal conductivity factor only improves 3 times." solar energy journal " (1998,19:186-190) " strengthening the research of heat-conductive characteristic in the solar energy absorber " the civilian described polyaniline/zeolite compound adsorbent in, its thermal conductivity factor also only improves 2~4 times, and mass-transfer performance descends to some extent.
Summary of the invention:
The objective of the invention is to propose a kind of compound adsorbent and preparation method thereof, can when significantly improving the adsorbent heat conductivility, still keep original mass-transfer performance.
The preparation method of adsorbent of the present invention/foamed aluminium composite adsorbing material adopts THROUGH METHOD; It is characterized in that: spherical zeolite granular or the sieve particle of diameter 3~6mm are filled in the mould to 20~60mm height; the salt particle that adds diameter<1mm in salt and 4: 6 ratio of absorbent particles heap volume ratio; the absorbent particles gap is filled evenly; being forced into 2~3atm compresses in advance; and be preheated to 500~600 ℃; in molten aluminum and 2: 8 ratio of absorbent particles heap volume ratio molten aluminum is poured into mould then; and be forced into 2~5atm; take out washing after to be cooled the solidifying salt particle dissolves is wherein washed out, promptly obtained adsorbent/foamed aluminium composite adsorbing material in 3 hours at 350 ℃ of constant temperature at last.
Adsorbent of the present invention/foamed aluminium composite adsorbing material; it is characterized in that: be made up of the fine-crystal spume aluminium alloy that accounts for volume fraction 10%~20% of filling in the zeolite granular that accounts for volume fraction 60%~65% or sieve particle and the gap thereof, adopting the stable state flat band method to measure its thermal conductivity factor is 1~4W/mK.
Because compound adsorbent preparation method of the present invention uses the spherical adsorbent paricles gap of diameter less than the particles filled diameter 3~6mm of the salt of 1mm, and pressurized treatments, the salt particle easily forms continuous phase, original salt particle position just forms netted open-end hole in water-washing process like this, reduced the use amount of metallic aluminium on the one hand, reduced the harmful effect that the metallic aluminium thermal capacitance lags behind to heat of adsorption, absorbent particles for inside provides unimpeded mass transfer channel simultaneously, makes the adsorbent mass-transfer performance influenced hardly.Metallic aluminium volume contraction when solidifying cooling understands nature and the absorbent particles combination is tight, therefore need not to add curing agent, just can reduce the heat transfer resistance between metal and the absorbent particles, also can overcome simultaneously and stop up the adsorbent surface micropore after using curing agent, reduce the shortcoming of absorption property.Metallic aluminium is that continuous phase distributes between the absorbent particles space, can obviously improve heat conductivility, than molecular sieve with zeolite granular is stacking bed exceeds tens times.The mechanical property excellence of foamed aluminium material can be used as the adsorbent support frame simultaneously, structural strength height, not yielding breakage.
The present invention uses the through-hole foam aluminum of volume ratio 10%~20% to be the heat transfer skeleton, composite zeolite particle or sieve particle, and the time processing moulding significantly improves its heat conductivility, and has higher mass-transfer performance, and manufacture craft is simple, and is with low cost.Can reduce the adsorption/desorption time greatly for the adsorbent refrigerator that uses zeolite or sieve adsorpting bed, improve the refrigeration machine performance.
The specific embodiment:
Embodiment 1:
Adsorbent in the present embodiment adopts spherical zeolite granular or spherical sieve particle.
With the spherical zeolite granular of diameter 3~6mm or spherical sieve particle be filled to highly in the high cylindrical die of 150mm to the 60mm height; the salt particle of pressing then about salt and absorbent particles heap volume ratio adding in 4: 6 diameter 0.5mm is filled its gap evenly; and be forced into 2~3atm and compress in advance; be preheated to 500~600 ℃ simultaneously; by molten aluminum and absorbent particles heap volume ratio 2: 8 molten aluminum is poured into mould then; and be forced into 2~5atm its seepage flow is gone in the particle voids; waiting to solidify cooling fully takes out the back; wash out after making wherein salt particle dissolves by washing; in the oven dry activation in 3 hours of 350 ℃ of following constant temperature, promptly obtain adsorbent/foamed aluminium composite adsorbing material at last.
Weigh before and after volume by measuring the gained material, the washing and according to the density calculation of salt, absorbent particles and aluminium as can be known, the adsorbent of gained/foamed aluminium composite adsorbing material is filled composition by the fine-crystal spume aluminium alloy of the occupied percent by volume 10%~20% in the gap between zeolite granular that accounts for percent by volume 60%~65% or the sieve particle.
The thermal conductivity factor that adopts the stable state flat band method to measure resulting compound adsorbent is 1~4W/mK.
Adopt the resulting compound adsorbent of the inventive method, owing to form the through-hole foam constructed of aluminium, adsorbate steam mass transfer channel is unimpeded, and mass-transfer performance is influenced hardly.
Claims (2)
1. the preparation method of adsorbent/foamed aluminium composite adsorbing material, it is characterized in that: the sieve particle of diameter 3~6mm is filled in the mould to 20~60mm height, the salt particle that adds diameter<1mm in salt and 4: 6 ratio of absorbent particles heap volume ratio, the absorbent particles gap is filled evenly, being forced into 2~3atm compresses in advance, and be preheated to 500~600 ℃, in molten aluminum and 2: 8 ratio of absorbent particles heap volume ratio molten aluminum is poured into mould then, and be forced into 2~5atm, the back of solidifying to be cooled is taken out washing salt particle dissolves is wherein washed out, at last 350 ℃ of constant temperature 3 hours.
2. adsorbent/foamed aluminium composite adsorbing material, it is characterized in that: be made up of the fine-crystal spume aluminium alloy that accounts for volume fraction 10%~20% of filling in sieve particle that accounts for volume fraction 60%~65% and the gap thereof, adopting the stable state flat band method to measure its thermal conductivity factor is 1~4W/mK.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100140234A CN1306996C (en) | 2004-02-03 | 2004-02-03 | A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100140234A CN1306996C (en) | 2004-02-03 | 2004-02-03 | A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1651133A CN1651133A (en) | 2005-08-10 |
| CN1306996C true CN1306996C (en) | 2007-03-28 |
Family
ID=34867865
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100140234A Expired - Fee Related CN1306996C (en) | 2004-02-03 | 2004-02-03 | A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1306996C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993414A (en) * | 2018-07-25 | 2018-12-14 | 南京工业大学 | Preparation method of MOFs-foam metal composite adsorbent |
Families Citing this family (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101844424B (en) * | 2010-03-26 | 2013-01-09 | 林灯 | Compound foamed aluminum particle board and manufacturing process thereof |
| DE102010030547A1 (en) | 2010-06-25 | 2011-12-29 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Pellets and process for their preparation |
| CN102120121B (en) * | 2011-01-11 | 2013-06-19 | 常州大学 | Oil gas adsorber |
| CN106669599B (en) * | 2017-01-09 | 2019-11-08 | 山东大学苏州研究院 | A kind of thermally conductive skeleton compound adsorbent of zeolite molecular sieve-and preparation method |
| CN109248672B (en) * | 2018-06-28 | 2022-01-14 | 霍尼韦尔特性材料和技术(中国)有限公司 | Composite material and preparation method and application thereof |
| CN113423244B (en) * | 2021-06-28 | 2022-06-21 | 哈尔滨工业大学 | Preparation method and application of aluminum-based liquid cooling heat dissipation structure |
| CN120703151B (en) * | 2025-08-27 | 2025-10-28 | 中北大学 | A method for measuring thermal conductivity of nano-adsorbent material in moisture absorption state |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4112358A1 (en) * | 1991-04-16 | 1992-10-22 | Bayerische Motoren Werke Ag | Latent heat store zeolite moulding - has metal foam substrate permeable to adsorbate with impermeable boundary surface |
| CN1173831A (en) * | 1995-02-06 | 1998-02-18 | G·J·布拉顿 | Adsorbent material |
| CN1266741A (en) * | 2000-04-06 | 2000-09-20 | 上海交通大学 | Lump zeolite adsorbent with excellent heat conductivity and adsorptivity |
| DE10047503A1 (en) * | 2000-09-21 | 2002-04-18 | Disa Tech Technologie Entwickl | Sorption reactor, for heat exchange in vehicle/building air conditioning systems, has a compound structure of zeolite and metal in a container together with an evaporator for steam |
-
2004
- 2004-02-03 CN CNB2004100140234A patent/CN1306996C/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4112358A1 (en) * | 1991-04-16 | 1992-10-22 | Bayerische Motoren Werke Ag | Latent heat store zeolite moulding - has metal foam substrate permeable to adsorbate with impermeable boundary surface |
| CN1173831A (en) * | 1995-02-06 | 1998-02-18 | G·J·布拉顿 | Adsorbent material |
| CN1266741A (en) * | 2000-04-06 | 2000-09-20 | 上海交通大学 | Lump zeolite adsorbent with excellent heat conductivity and adsorptivity |
| DE10047503A1 (en) * | 2000-09-21 | 2002-04-18 | Disa Tech Technologie Entwickl | Sorption reactor, for heat exchange in vehicle/building air conditioning systems, has a compound structure of zeolite and metal in a container together with an evaporator for steam |
Non-Patent Citations (6)
| Title |
|---|
| Enhancement of heat and mass transfer in silica-expandedgraphite composite blocks for adsorption heat pumps: Part I.Characterization of the composite blocks Tai.Hee Eun,et al,International Journal of Refrigeration,Vol.23 2000 * |
| Enhancement of heat and mass transfer in silica-expandedgraphite composite blocks for adsorption heat pumps: Part I.Characterization of the composite blocks Tai.Hee Eun,et al,International Journal of Refrigeration,Vol.23 2000;Heat Transfer intensification in fixed bed adsorbers J.J.Guilleminot,et al,Heat Recovery Systems & CHP,Vol.13 No.4 1993;Preparation and properties of an electrically heatablealuminium foam/zeolite composite-Franziska Scheffler,et al,Microporous and Mesoporous Materials,Vol.67 No.1 2004;渗流法制备泡沫铝合金工艺的研究 程和法等,轻合金加工技术,第29卷第1期 2001;太阳能吸附器中强化热传导性能的实验研究 朱冬生等,太阳能学报,第19卷第2期 1998 * |
| Heat Transfer intensification in fixed bed adsorbers J.J.Guilleminot,et al,Heat Recovery Systems & CHP,Vol.13 No.4 1993 * |
| Preparation and properties of an electrically heatablealuminium foam/zeolite composite-Franziska Scheffler,et al,Microporous and Mesoporous Materials,Vol.67 No.1 2004 * |
| 太阳能吸附器中强化热传导性能的实验研究 朱冬生等,太阳能学报,第19卷第2期 1998 * |
| 渗流法制备泡沫铝合金工艺的研究 程和法等,轻合金加工技术,第29卷第1期 2001 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108993414A (en) * | 2018-07-25 | 2018-12-14 | 南京工业大学 | Preparation method of MOFs-foam metal composite adsorbent |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1651133A (en) | 2005-08-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN112691645B (en) | Carbon aerogel/metal organic framework composite material, preparation method thereof and application thereof in gas storage | |
| CN108079934B (en) | A kind of composite material and preparation method thereof | |
| CN1306996C (en) | A kind of adsorbent/foam aluminum composite adsorption material and preparation method thereof | |
| CN101961644B (en) | Chloride-carbonaceous skeleton composite adsorbent and preparation method thereof | |
| CN113117647B (en) | Foam metal supporting adsorption material and preparation method thereof | |
| CN102071333B (en) | Method for preparing foamed TiAl intermetallic compound | |
| CN105056896A (en) | MoFs adsorbent and application thereof | |
| CN104726745A (en) | Ti-Zr based light-weight high-capacity hydrogen absorption material, and preparation method and application method thereof | |
| CN103526064A (en) | Preparation method for foamy copper | |
| CN106905928B (en) | Encapsulated phase change energy storage composite material with ultra-high thermal conductivity and its processing technology | |
| Atakan et al. | Adsorption kinetics and isotherms of zeolite coatings directly crystallized on fibrous plates for heat pump applications | |
| CN107603571B (en) | Preparation of shaped expanded graphite-based erythritol intermediate-temperature composite phase-change heat storage material | |
| CN101113323A (en) | Foam heat storage and method for preparing the same | |
| Kiplagat et al. | Enhancement of heat and mass transfer in solid gas sorption systems | |
| CN114032073A (en) | Preparation method of slag expanded bead composite phase-change material | |
| CN111205827A (en) | A method of using activated carbon to prevent the loss of molten salt phase change heat storage material | |
| CN118580838A (en) | Preparation method of erythritol expanded graphite high thermal conductivity shaped composite phase change material | |
| Strelova et al. | Dynamics of water vapour sorption on composite LiCl/(silica gel): An innovative configuration of the adsorbent bed | |
| CN115074089A (en) | Preparation method of high-heat-conductivity modular phase-change heat storage unit | |
| CN101717873B (en) | Powder forging and molding method for preparing porous amorphous alloy block material | |
| CN112777564A (en) | Magnesium-nickel-petroleum coke active carbon composite hydrogen storage material and preparation method thereof | |
| CN101274266A (en) | Preparation method of sintered zeolite molecular sieve finned single tube for shell-and-tube adsorption bed | |
| CN110065942B (en) | A kind of rice-based granular microporous/ultra-microporous carbon material and preparation method thereof | |
| CN113621348B (en) | A high thermal conductivity phase change material based on chitin-derived carbon and its preparation method and heat storage application | |
| Liu et al. | The heat and mass transfer performance of facile synthesized silica gel/carbon-fiber based consolidated composite adsorbents developed by freeze-drying method |
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 | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20070328 Termination date: 20100203 |