Hydrogen-hydride absorption systems and methods for refrigeration and heat pump cycles

[5. An absorption system as defined in claim 1 wherein said means for supplying heat to said first and second reactor means comprises:

• heat exchanger means;
• a feed pump means connected to said heat exchanger means;
• and
• a valve-containing conduit system connected between said feed pump means, said heat exchanger means and said first and second reactor means for circulating a heat exchange fluid from said heat exchange means and feed pump means to said reactor means.]

[6. An absorption system as defined in claim 1 wherein said means for removing heat from each of the subsystem reactor means comprises:

• a heat exchanger;
• a feed pump connected to said heat exchanger;
• and
• a conduit system containing valving and connected between said feed pump, heat exchanger and each reactor means of each of said subsystems for circulating a heat exchange fluid between the heat exchanger, feed pump
• and the reactor means of the respective subsystems.]

[9. A method for deriving refrigeration from a hydrogen absorption system which includes two subsystems each containing a plurality of hydride-dehydride reactors, which method comprises:

• combining hydrogen gas with a first hydride-forming material in a reactor of one of said subsystems under conditions of a temperature, T.sub.1, and a pressure, P.sub.1, such that a first hydride saturated with, and in equilibrium with, hydrogen gas is formed, as the thus combined hydrogen gas is desorbed from a second hydride in a reactor of the second subsystem at a refrigeration temperature, T.sub.2, lower than T.sub.1, and a pressure, P.sub.2, slightly greater than P.sub.1, wherein the heat necessary to desorb the second hydride is the refrigeration load;
• concurrently heating the first and second hydrides at constant volume by recovering sensible heat from a different reactor in their respective subsystems;
• then
• further heating the first hydride at constant volume to a temperature, T.sub.3, and a pressure, P.sub.3, which are substantially higher than T.sub.1, and P.sub.1 ;
• and
• further heating the second hydride at constant volume to a temperature, T.sub.1, and a pressure slightly lower than P.sub.3 ;
• heating the first hydride to desorb hydrogen gas at a temperature, T.sub.3, and a pressure, P.sub.3 ;
• absorbing the last-mentioned desorbed hydrogen gas in the hydridable material derived from said second hydride;
• concurrently cooling the first and second hydrides at constant volume by transferring heat to a reactor in each of the respective subsystems;
• further cooling the first hydride at constant volume by a heat exchange fluid;
• cooling the second hydride by dehydriding the second hydride by desorption of hydrogen therefrom;
• and
• cyclically repeating the foregoing steps.]

[13. A method for deriving a heat pump effect from a hydrogen absorption system comprising:

• combining hydrogen gas with a first hydride-forming material under conditions of temperature, T.sub.1, and pressure, P.sub.1, such that a first hydride saturated with and in equilibrium with hydrogen gas is formed as the hydrogen gas is desorbed from a second hydride at a temperature, T.sub.2, substantially lower than T.sub.1, and a pressure, P.sub.2, slightly greater than P.sub.1, wherein the heat of absorption of the first hydride is the heat pump effect;
• partial cooling of the first and second hydrides at constant volume by transferring heat to a reactor in each of their respective systems;
• further cooling the first hydride by desorption;
• cooling the second hydride at constant volume by a heat exchange fluid;
• heating the first hydride to desorb hydrogen gas at a temperature, T.sub.2, and a pressure, P.sub.4, substantially lower than P.sub.1, and combining the hydrogen gas in the second hydride-forming material at a temperature, T.sub.3, substantially lower than T.sub.2, and a pressure, P.sub.3, slightly lower than P.sub.4 ;
• partially heating the first and second hydrides at constant volume by recovering heat from a reactor in their respective systems;
• further heating the first hydride by absorption;
• heating the second hydride at constant volume to the temperature, T.sub.2, and pressure, P.sub.2 ;
• and
• cyclically repeating the foregoing steps.]

[17. A method for deriving refrigeration from a hydrogen absorption system comprising:

• establishing a first group of first reaction zones having a first hydridable material in at least one of said first reaction zones, and a hydride formed from said first hydridable material in another of said first reaction zones;
• establishing a second group of second reaction zones having a second hydridable material in at least one of said second reaction zones, and a hydride formed from said second hydridable material in at least one other of said second reaction zones, said second hydridable material having a capability of producing an equilibrium pressure of hydrogen higher than the equilibrium pressure of hydrogen produced by said first hydridable material in said first reaction zones when both said first and second hydridable materials are at the same equilibrium temperature;
• transferring heat from a refrigeration medium to the one of said second reaction zones containing the hydride of said second hydridable material to desorb hydrogen gas therefrom at a refrigeration temperature T.sub.2, and in a pressure P.sub.2, wherein the heat necessary to desorb hydrogen gas from the hydride of the second hydridable material is the refrigeration load;
• transferring desorbed hydrogen gas from said second reaction zone containing a hydride of said second hydridable material undergoing desorption of the hydrogen gas from the hydride therein by the cooling of said refrigeration medium, to the first hydridable material in said one of said first reaction zones;
• combining said transferred hydrogen gas with said first hydridable material in said one of said first reaction zones under conditions of a temperature, T.sub.1, and a pressure, P.sub.1, which is less than P.sub.2, such that a hydride of said first hydridable material in said one first reaction zone which is saturated with, and in equilibrium with, hydrogen gas is formed with concurrent exothermal release of thermal energy;
• then
• concurrently increasing the temperature of the desorbed material in said one other of said second reaction zones, and concurrently, increasing the temperature of the hydride material formed in said one first reaction zone by the use of sensible heat supplied from a second of the reaction zones in the respective groups in which said one other of said second reaction zones, and said one of said first reaction zones are located;
• further heating the hydride of said first hydridable material at constant volume to a temperature, T.sub.3, and a pressure, P.sub.3, which temperature, T.sub.3, and pressure, P.sub.3, are higher than T.sub.1 and P.sub.1, respectively.
• further heating the hydride of the second hydridable material in said one other of said second reaction zones at constant volume to a temperature, T.sub.1, and a pressure lower than P.sub.3 ;
• terminating the constant volume restriction on the hydride of said first hydridable material in said one reaction zone of said first group and concurrently desorbing hydrogen gas therefrom by continuing to heat the hydride of said first hydridable material in said one reaction zone of said first group at a temperature, T.sub.3, and pressure, P.sub.3, with concurrent volumetric expansion of the desorbed hydrogen gas;
• transferring the desorbed hydrogen gas from said one reaction zone of said first group of reaction zones to the second hydridable material in said one other reaction zone of said second group of reaction zones;
• combining said last-mentioned transferred hydrogen gas with said second hydridable material in said other reaction zone of said second group and maintaining an equilibrium pressure lower than P.sub.3 by transferring heat to an external heat exchange medium, to increase the temperature in said one other reaction zone of said second group while retaining constant volume in said one other reaction zone;
• then
• concurrently decreasing the temperature of the materials in said one reaction zone of said first group, and in said one other reaction zone of said second group by transferring sensible heat therefrom to a different one of the respective first and second reaction zones in the respective first and second groups containing said one reaction zone and said one other reaction zone;
• further cooling the material in said one reaction zone of said first group while retaining said one reaction zone at constant volume;
• further cooling the material in said one other reaction zone of said second group by desorbing hydrogen gas from the material therein;
• and
• cyclically repeating the foregoing steps.]

An absorption system including:

• hydrogen
• a first hydride-dehydride subsystem including first reactor means inclusive of a plurality of reactors;
• a first hydridable material in said first reactor means for forming a first hydride by reaction with said hydrogen gas;
• a second hydride-dehydride subsystem including second reactor means inclusive of a plurality of reactors;
• a second hydridable material different from said first hydridable material in said second reactor means for forming a second hydride by reaction with said hydrogen gas;
• means for periodically transferring said hydrogen gas between said first and second reactor means;
• means for supplying heat to said first reactor means and said second reactor means in alternating sequence for effecting chemical compression and dehydriding of the hydrides of said first and second hydridable materials;
• a conduit system interconnecting the reactors in each of said first and second reactor means;
• pump means associated with each of said conduit systems for circulating a heat exchange fluid through each of said conduit systems between two of the reactors in each of said first and second reactor means at a time when one of said two reactors is undergoing activation of the hydridable material therein, and the other of said two reactors is undergoing deactivation of a hydride of the hydridable material therein.
• means for removing heat from the reactor means in each of said subsystems.

A method for deriving a heat pump effect from a hydrogen absorption system comprising:

• (A) combining hydrogen gas with a first hydride-forming material under conditions of temperature, T.sub.1, and pressure, P.sub.1, such that a first hydride is formed as said hydrogen gas is desorbed from a hydride of a second hydride-forming material, different from said first hydride-forming material, at a temperature, T.sub.2, substantially lower than T.sub.1, and a presusre, P.sub.2, slightly greater than P.sub.1, wherein the heat of absorption of the first hydride is the heat pump effect;
• (B) cooling the resultant hydride of said first hydride-forming material and said second hydride-forming material while minimizing hydrogen transfer therebetween;
• (C) heating said hydride of said first hydride-forming material to desorb hydrogen gas therefrom at a temperature lower than T.sub.1 to thereby provide hydrogen gas for the rehydriding of said second hydride-forming material;
• and
• (D) thereafter, bringing the hydride of said second hydride-forming material to the condition of T.sub.2 P.sub.2 so as to enable repetition of the steps of said method.

A method for deriving refrigeration from a hydrogen absorption system comprising:

• (a) establishing a first group of first reaction zones having a first hydridable material in at least one of said first reaction zones, and a hydride formed from said first hydridable material in another of said first reaction zones;
• (b) establishing a second group of second reaction zones having a second hydridable material in at least one of said second reaction zones, and a hydride formed from said second hydridable material in at least one other of said second reaction zones, said second hydridable material having a capability of producing an equilibrium pressure of hydrogen higher than the equilibrium pressure of hydrogen produced by said first hydridable material in said first reaction zones when both said first and second hydridable materials are at the same equilibrium temperature;
• (c) transferring heat from a refrigeration medium to the one of said second reaction zones containing the hydride of said second hydridable material to desorb hydrogen gas therefrom at a refrigeration temperature and at a pressure P.sub.2, wherein the heat necessary to desorb hydrogen gas from the hydride of the second hydridable material is the refrigeration load;
• (d) transferring desorbed hydrogen gas from said second reaction zone containing a hydride of said second hydridable material undergoing desorption of the hydrogen gas from the hydride therein by the cooling of said refrigeration medium, to the first hydridable material in the said one of said first reaction zones;
• (e) combining said transferred hydrogen gas with said first hydridable material in said one of said first reaction zones under conditions of a temperature, T.sub.1, and a pressure, P.sub.1, which is less than P.sub.2, such that a hydride of said first hydridable material in said one first reaction zone is formed with concurrent exothermal release of thermal energy;
• then
• (f) concurrently increasing the temperature of the desorbed material in said one other of said second reaction zones, and concurrently, increasing the temperature of the hydride material formed in said one first reaction zone by the use of sensible heat supplied from a second of the reaction zones in the respective groups in which said one other of said second reaction zones, and said one of said first reaction zones are located;
• (g) further heating the hydride of said first hydridable material at constant volume to a temperature, T.sub.3, and a pressure, P.sub.3, which temperature, T.sub.3, and pressure, P.sub.3, are higher than T.sub.1 and P.sub.1, respectively;
• (h) further heating the material in said one other of said second reaction zones at constant volume to a temperature, T.sub.1, and a pressure lower than P.sub.3 ;
• (i) terminating the constant volume restriction on the hydride of said first hydridable material in said one reaction zone of said first group and concurrently desorbing hydrogen gas therefrom by continuing to heat the hydride of said first hydridable material in said one reaction zone of said first group at a temperature, T.sub.3, and pressure, P.sub.3, with concurrent volumetric expansion of the desorbed hydrogen gas;
• (j) transferring the desorbed hydrogen gas from said one reaction zone of said first group of reaction zones to the second hydridable material in said one other reaction zone of said second group of reaction zones;
• (k) combining said last-mentioned transferred hydrogen gas with said second hydridable material in said other reaction zone of said second group and maintaining a pressure lower than P.sub.3 by transferring heat to an external heat exchange medium, to increase the temperature in said one other reaction zone of said second group while retaining constant volume in said one other reaction zone;
• then
• (l) concurrently decreasing the temperature of the materials in said one reaction zone of said first group, and in said one other reaction zone of said second group by transferring sensible heat therefrom to a different one of the respective first and second reaction zones in the respective first and second groups containing said one reaction zone and said one other reaction zones;
• (m) further cooling the material in said one reaction zone of said first group while retaining said one reaction zone at constant volume;
• (n) further cooling the material in said one other reaction zone of said second group by desorbing hydrogen gas from the material therein;
• and
• (o) cyclically repeating steps c through n.