Apparatus and method for energy recovery

Abstract

There is provided a heating system for a building comprising; i) a heater; ii) a media flow passage through which a medium heated by the heater passes in order to distribute heat through the building; and iii) a heat recovery apparatus for recovering latent heat of adsorption from a humid gas. The heat recovery apparatus comprises a) a gas flow passage connected at one end to a source of humid gas; b) a desiccant material provided within the gas flow passage such that the humid gas contacts the desiccant material and water vapour is adsorbed releasing latent heat of adsorption; wherein the media flow passage and gas flow passage are in heat exchanging relationship, such that when the desiccant material adsorbs water vapour from the exhaust gas the latent of the adsorption is at least partially transmitted to the medium.

1 . A heating system for a building comprising;
 i) a heater;   ii) a media flow passage through which a medium heated by the heater passes in order to distribute heat through the building; and   iii) a heat recovery apparatus for recovering latent heat of adsorption from a humid gas, comprising;
 a) a gas flow passage connected at one end to a source of humid gas; and 
 b) a desiccant material provided within the gas flow passage such that the humid gas contacts the desiccant material and water vapour is adsorbed releasing latent heat of adsorption; wherein 
   the media flow passage and gas flow passage are in heat exchanging relationship, such that when the desiccant material adsorbs water vapour from the exhaust gas the latent of adsorption is at least partially transmitted to the medium.   
     
     
         2 . The heating system of  claim 1  wherein the humid gas source comprises a humid gas of a room of the building, in which there is a supply of humidity, for example respiration. 
     
     
         3 . The heating system of  claim 1  wherein the heater is an electric heater. 
     
     
         4 . The heating system of  claim 1  wherein the heater is a carbonaceous-fuel-fired heater and the humid gas source comprises an exhaust gas of the heater. 
     
     
         5 . The heating system of  claim 1  wherein at least 1000 kg, more preferably at least 5000 kg, of desiccant is provided in the gas flow passage. 
     
     
         6 . The heating system of  claim 1  wherein the desiccant material is a solid desiccant material selected from a group consisting of silica gel; silica gel beads; activated alumina; activated bauxite; or one of more molecular sieves. 
     
     
         7 . The heating system of  claim 1  wherein the building is a residential or commercial dwelling. 
     
     
         8 . The heating system of  claim 1  comprising a regenerating-gas flow path for bringing a supply of a regenerating-gas into contact with the desiccant material, wherein the regenerating gas is of a suitable humidity and temperature to effect at least partial dehydration of the desiccant. 
     
     
         9 . A method of heating a building, comprising the steps of;
 i) heating a distribution-medium by means of a heater;   ii) circulating the heated distribution-medium through the building to distribute the heat; and   iii) recovering the latent heat of adsorption from a humid gas by;
 a) contacting the humid gas with a desiccant material such that water vapour is adsorbed by the desiccant and the latent heat of adsorption is released as sensible heat; and 
 b) heat exchanging the desiccant material and/or the gas with the distribution-medium such that at least a portion of the released sensible heat is passed to the medium. 
   
     
     
         10 . The method of  claim 9  wherein the humid gas source comprises a humid gas of a room of the building, in which there is a supply of humidity, for example respiration. 
     
     
         11 . The method of  claim 9  wherein the heater is an electric heater. 
     
     
         12 . The method of  claim 9  wherein the heater is a carbonaceous-fuel-fired heater and the humid gas source comprises an exhaust gas of the heater 
     
     
         13 . The method of  claim 9  wherein at least 1000 kg, more preferably at least 5000 kg, of desiccant is provided in the gas flow passage. 
     
     
         14 . The method of  claim 9  wherein the desiccant material is a solid desiccant material selected from a group consisting of silica gel; silica gel beads; activated alumina; activated bauxite; or one of more molecular sieves. 
     
     
         15 . The method of  claim 9  wherein the building is a residential or commercial dwelling. 
     
     
         16 . The method of  claim 9  wherein during the step of contacting the humid gas with the desiccant material, the desiccant material is maintained at a temperature between 20° C. to 70° C., more preferably 30° C. to 60° C. and most preferably 40° C. to 50° C. 
     
     
         17 . The method of  claim 9  comprising the step of regenerating the desiccant by effecting at least partial dehydration thereof. 
     
     
         18 . The method of  claim 17  wherein regeneration of the desiccant is effected by contacting the desiccant with a dehydrating gas. 
     
     
         19 . The method of  claim 17  wherein regeneration of the desiccant is at least partially effected by heating the desiccant using one or more energy sources selected from;
 i) solar energy; 
 ii) outside air of a suitable temperature and humidity; 
 iii) waste-heat from refrigerator units and/or air-conditioning units. 
 
     
     
         20 . The method of  claim 17  wherein the steps of; i) contacting humid gas with the desiccant; and ii) regeneration of the desiccant, do not take place simultaneously.