US2006186669A1PendingUtilityA1

Power generation methods and systems

Assignee: RUGGIERI FRANKPriority: Apr 16, 2002Filed: Jan 17, 2006Published: Aug 24, 2006
Est. expiryApr 16, 2022(expired)· nominal 20-yr term from priority
F24D 2101/10F24D 2103/13F24D 2105/00F24D 18/00Y02E20/14F01K 17/02F22B 21/26F01K 25/065
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Claims

Abstract

Thermodynamic energy methods and systems that provides all electrical energy and heat needs of a single residential house, commercial business or office building. The system is small enough to be stored inside the house or building. The system can generate excess electrical energy which can be sold over a power grid and allow for the house owner, building owner or energy provider (utility company) to provide income. The method and system can have combined energy conversion efficiency up to approximately 97%. Components can include amorphous materials, and the mono-tube steam generator boiler which is explosion proof when punctured, and only emits a puff of steam when punctured. The tubes can be built to pressure vessel code. The invention can use steam generators to power A/C units, domestic hot water, hot water air space heaters, other loads such as pools and spas and underground piping to eliminate ice and snow. Additionally, the invention can be used to power vehicles such as cars, and the like. Other embodiments can use thermodynamic energy methods and systems that provides electrical energy and heat needs of a residence, commercial business, or office building, that include supertropically expanding ammonia vapor against a vacuum, as generated by chemosorption, in order to convert moderate amounts of heat into mechanical energy at high efficiencies. A supertropic package system can include a source of ammonia/water, a thermal generator for heating the source of ammonia/water and generating ammonia gas, a positive displacement device for expanding the gas, and generating electricity from a power source driven by the expander.

Claims

exact text as granted — not AI-modified
1 . A method of converting moderate amounts of heat into mechanical energy at high efficiencies, comprising the steps of: 
 supertropically expanding a gas vapor against a vacuum, as generated by chemosorption, in order to convert moderate amounts of heat into mechanical energy at high efficiencies.    
   
   
       2 . The method of  claim 2 , further comprising the step of: 
 providing ammonia as the gas vapor.    
   
   
       3 . A supertropic energy generating package system, comprising: 
 a gaseous source;    a thermal generator for heating the source of ammonia/water and generating a gas;    a scroll expander for expanding the gas; and    a power source being driven by the expanding gas, the power source generating electricity therefrom.    
   
   
       4 . The system of  claim 3 , wherein the gaseous source includes: 
 ammonia and water.    
   
   
       5 . A supertropic expansion device, for converting heat into mechanical energy, comprising: 
 means for expanding vapors close to, or being at saturation condition against a lower pressure than atmospheric, at polytrophic expansion conditions, as generated otherwise than by surface condensation.    
   
   
       6 . The device according to  claim 5 , further comprising: 
 means for achieving said polytrophic expansion conditions internally in a rotary sliding vane machine.    
   
   
       7 . The device according to  claim 5 , further comprising: 
 means for achieving said polytrophic expansion conditions in a displacement device, by injection of fluids therein.    
   
   
       8 . A method of generating electrical power from ammonia, comprising the steps of: 
 heating ammonia gas;    expanding the heated ammonia by an expander to a larger volume while dropping temperature of the ammonia gas;    driving a motor by the expander; and    generating electricity from the motor.    
   
   
       9 . The method of  claim 8 , wherein the heating step includes the steps of: 
 heating the ammonia to approximately 700 F at approximately 75 psi.    
   
   
       10 . The method of  claim 8 , wherein the expanding step includes the steps of: 
 increasing the volumne of the heated ammonia gas to approximately 3.6 times its original input while dropping temperature to minus approximately 70 F.    
   
   
       11 . The method of  claim 8 , wherein the driving step includes the step of: 
 rotating a shaft attached to the motor by the expander.    
   
   
       12 . The method of  claim 8 , further comprising the step of: 
 providing an alternator as the motor.    
   
   
       13 . The method of  claim 8 , further comprising the step of: 
 collecting fluid from the expander in a reservoir    
   
   
       14 . The method of  claim 13 , wherein the fluid can be a mixture of approximately 60% liquid and approximately 40% vapor.  
   
   
       15 . The method of  claim 13 , further comprising the step of: 
 passing the liquid and the vapor from the receiver to an absorber.    
   
   
       16 . The method of  claim 15 , further comprising the steps of: 
 creating a low pressure in the absorber which allows the temperature to drop from the expander; and    causing the expander to work in a substantial temperature differential for a high Carnot efficiency, and effecting a supertropic effect therefrom.    
   
   
       17 . The method of  claim 16 , wherein the low pressure is approximately 3 psi, and the temperature drop in the expander is minus approximately 70 F, the temperature differential is approximately 770 F, and the Carnot efficiency is approximately 62.6%  
   
   
       18 . The method of  claim 16 , further comprising the step of: 
 cycling liquid back to the absorber by a desorber to increase efficiency of the electricity being generated.    
   
   
       19 . A method of generating electrical energy from an expanding gas, comprising the steps of: 
 heating fluid into a gas;    supertropically expanding the gas by an expander;    driving an electric generator by the expander;    generating electricity from the electric generator;    condensing the gas into a liquid;    passing the liquid through an absorber, a regenerator, and a desorber in a closed cycle to continuously provide a vacuum condition for the supertropic expansion.

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