| 2677664 | Composition of matter for the storage of heat | May, 1954 | Telkes | 252/70 |
| 2706716 | Heat storage material | April, 1955 | Howe et al. | 252/70 |
| 2856506 | Method for storing and releasing heat | October, 1958 | Telkes | 219/39 |
| 3536059 | CHEMICAL HEAT SOURCE FOR DIVERS | October, 1970 | Hearst | 126/204 |
| 3973552 | Method of storing and releasing thermal energy | August, 1976 | Ervin | 126/271 |
| 4003426 | Heat or thermal energy storage structure | January, 1977 | Best et al. | 165/53 |
| 4109702 | Energy storage and retrieval as heat | August, 1978 | Greene | 165/1 |
| 4117882 | Process and apparatus for heat exchange | October, 1978 | Shurcliff | 165/104S |
| DE2550106 | May, 1976 | |||
| FR2396061 | January, 1979 | |||
| JP5090585 | July, 1975 | |||
| JP5143387 | April, 1976 | |||
| JP5170193 | June, 1976 | |||
| JP5176183 | July, 1976 | |||
| JP51126980 | November, 1976 | COMPOSITES FOR HEAT ACCUMULATOR MATERIAL | ||
| JP5319183 | February, 1978 | |||
| JP5314785 | May, 1978 | 252/70 | ||
| JP5370989 | June, 1978 | |||
| GB2001096 | January, 1979 | |||
| SU568669 | September, 1977 |
The invention relates to reversible liquid/solid phase change compositions. More particularly, the invention relates to Mg(NO 3 ) 2 .6H 2 O/NH 4 NO 3 phase change compositions containing additives to modify the supercooling properties of the Mg(NO 3 ) 2 .6H 2 O/NH 4 NO 3 liquid phase.
Mg(NO 3 ) 2 .6H 2 O/NH 4 NO 3 forms a eutectic mixture which phase changes at about 52° C. (126° F.) releasing or alternately absorbing a substantial quantity of latent heat of fusion. Such properties make the material an excellent choice as a heat storage medium for use in solar energy space heating applications. In order to improve the material for such uses, however, there exists a need to develop additives or a series of additives to suppress the inherent supercooling properties of the Mg(NO 3 ) 2 .6H 2 O/NH 4 NO 3 liquid phase, and particularly additives which are highly effective in small amounts.
"Hydrated Mg(NO 3 ) 2 /NH 4 NO 3 " means aqueous based, reversible liquid/solid phase change compositions, which exclusive of any additives or impurities, contain in admixture from about 60 to 63 weight percent hydrated Mg(NO 3 ) 2 of principally Mg(NO 3 ) 2 .6H 2 O, and the balance NH 4 NO 3 (to 100 weight percent). The preferred composition is a hydrate mixture having a melt/freeze temperature of about 52° C. (126° F.) and which contain about 61.5 weight percent Mg(NO 3 ) 2 .6H 2 O, 38.5 weight percent NH 4 NO 3 .
"Supercooling" refers to a generally inherent discrepancy between the temperature at which freezing initiates and the thawing temperature of a given hydrated Mg(NO 3 ) 2 /NH 4 NO 3 composition, when cooled and heated under quiet conditions.
"Additive(s)" includes, in addition to the nucleating additives specified herein, precursors of such additives nondetrimental to the purpose of the invention.
The invention is the discovery of a new class of highly active nucleating additives for hydrated Mg(NO 3 ) 2 /NH 4 NO 3 compositions. The invention more particularly is a composition comprising hydrated Mg(NO 3 ) 2 /NH 4 NO 3 and which includes as a nucleating additive to such composition, one or more of the group of MgO, CaO, Mg(OH) 2 , and Ca(OH) 2 added in an amount effective to suppress the supercooling properties of the hydrated Mg(NO 3 ) 2 /NH 4 NO 3 liquid phase. Sufficient of the additive(s) is present in the preferred practice of the invention to suppress supercooling to no greater than about 2° C. taken on an averaging basis over repeated cycles.
The effective amount of the additive is determined by testing a given composition over repetitive phase change cycles. A given nucleating additive, if present in an insufficient amount may, for example, exhibit only temporary effectiveness. Such behavior is overcome by adding slightly greater amounts of that given additive.
The compositions hereof are ideally packaged in individual encapsulating means for use in conjunction with solar heating systems. Exemplary of suitable and known encapsulating means for the heat storage compositions hereof are water impervious foils of plastic/metal laminates. Also, closed cell plastic foams have been suggested in which the heat storage composition may be encapsulated within the cells of the foam structure, as illustrated, for example, in U.S. Pat. No. 4,003,426, incorporated herein by reference. Yet other useful encapsulating means are metal or plastic cans, such as inexpensive aerosol cans; metal or plastic pipe, such as extruded polyethylene pipe; and the like. Further details respecting such encapsulating means are given in Report Nos. ORO/5217-8 and NSF RANN SE C906 FR 76 1, both available from the National Technical Information Service, Springfield, Virginia, and fully incorporated herein by reference .
The data of the Table below are generated by preparing hydrated Mg(NO 3 ) 2 /NH 4 NO 3 samples according to the ratios indicated, and wherein the mixed samples of each specified ratio are placed into a two-ounce glass vial, which is then heated to greater than 70° C. under agitation to achieve a uniform dispersion or admixture. A glass-encased thermocouple is inserted through the cap of each vial to measure temperature changes at the center of each sample prior to, during and after freezing. The cooling temperature is controlled and maintained within the range of about 20° C.-25° C. (room temperature). Sample No. 16, below, is a control sample, whereas Sample Nos. 7-15 are comparative examples outside the scope of the invention.
| TABLE |
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| Super- Additive No. of cooling Sample Material wt. % Tests Ave., °C. |
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| 1 28.44g Mg(NO 3 ) 2 + Mg(OH) 2 0.1 6 6.8 30.80g NH 4 NO 3 + 20.76g H 2 O 2 28.44g Mg(NO 3 ) 2 + " 0.5 132 1.3 30.80g NH 4 NO 3 + 20.76g H 2 O 3 28.44g Mg(NO 3 ) 2 + MgO 0.1 131 1.8 30.80g NH 4 NO 3 + 20.76g H 2 O 4 28.44g Mg(NO 3 ) 2 + Ca(OH) 2 0.1 3 4.0 30.80g NH 4 NO 3 + 20.76g H 2 O 5 28.44g Mg(NO 3 ) 2 + " 0.5 113 1.7 30.80g NH 4 NO 3 + 20.76g H 2 O 6 28.44g Mg(NO 3 ) 2 + CaO 0.1 40 2.8 30.80g NH 4 NO 3 + 20.76g H 2 O 7 28.44g Mg(NO 3) 2 + CaSO 4 0.5 5 4.8 30.80g NH 4 NO 3 + 20.76g H 2 O 8 28.44g Mg(NO 3 ) 2 + Sr(OH) 2 0.1 3 4.3 30.80g NH 4 NO 3 + 20.76g H 2 O 9 28.44g Mg(NO 3 ) 2 + " 0.5 5 5.2 30.80g NH 4 NO 3 + 20.76g H 2 O 10 28.44g Mg(NO 3 ) 2 + SrCO 3 0.5 5 2.8 30.80g NH 4 NO 3 + 20.76g H 2 O 11 28.44g Mg(NO 3 ) 2 + Ba(OH) 2 0.1 2 6.0 30.80g NH 4 NO 3 + 20.76g H 2 O 12 28.44g Mg(NO 3 ) 2 + " 0.5 3 4.0 30.80g NH 4 NO 3 + 20.76g H 2 O 13 28.44g Mg(NO 3 ) 2 + BaO 0.5 4 2.8 30.80g NH 4 NO 3 + 20.76g H 2 O 14 28.44g Mg(NO 3 ) 2 + CuSO 4 0.5 5 5.9 30.80g NH 4 NO 3 + 20.76g H 2 O 15 28.44g Mg(NO 3 ) 2 + ZnSO 4 0.5 5 5.6 30.80g NH 4 NO 3 + 20.76g H 2 O 16 28.44g Mg(NO 3 ) 2 + None -- 3 8.3 30.80g NH 4 NO 3 + 20.76g H 2 O |
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It is understood that other nucleating additives than claimed herein and particularly the less effective additives of the comparative examples (Sample Nos. 7-15) may be used in conjunction with the highly active additives of the invention to prepare improved Mg(NO 3 ) 2 .6H 2 O/NH 4 NO 3 phase change compositions. While the data also illustrate that very little of the highly effective species of additives produce marked benefits, such additives may be incorporated in larger amounts, but preferably would not exceed the amount of about 2.0 weight percent of the weight of the phase change composition.