초록

An aqua-ammonia absorption cooling and/or heating system actively controls the flow of weak liquor from the generator to the absorber, using one or more valves operated in response to weak liquor temperature, and/or pressure and/or concentration.

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1. An aqua-ammonia absorption cooling and/or heating apparatus comprising: an absorber assembly, a generator assembly, a condenser, an evaporator, a refrigerant loop for directing refrigerant between said absorber assembly, generator assembly, condenser and evaporator, an absorption fluid loop for

1. An aqua-ammonia absorption cooling and/or heating apparatus comprising: an absorber assembly, a generator assembly, a condenser, an evaporator, a refrigerant loop for directing refrigerant between said absorber assembly, generator assembly, condenser and evaporator, an absorption fluid loop for directing absorption fluid between said absorber assembly and said generator assembly, said absorption fluid loop including first piping for directing ammonia-rich absorption fluid from the absorber assembly to the generator assembly and second piping for directing ammonia-weak absorption fluid from the generator assembly to the absorber assembly, a valve assembly comprising one or more first valves cooperating with the second piping for controlling the flow rate of weak absorption fluid therein, and a temperature-sensing bulb in thermal contact with ammonia-weak absorption fluid in the generator assembly for opening and/or closing a first valve in response to the sensed temperature of the ammonia-weak absorption fluid, said valve assembly including a movable member for controlling the opening and closing thereof and having a first side exposed to the bulb pressure and a second side exposed to generator pressure or pressure of the ammonia-weak absorption fluid from the generator, wherein a first valve is opened and closed in response to pressure differential between the first and second side of the movable member. 2. An apparatus of claim 1 wherein said condenser and evaporator comprise first and second heat exchangers, respectively, each capable of functioning as a condenser or an evaporator, said apparatus having one or more second valves cooperating with said refrigerant loop for selectively reversing the flow of refrigerant to and from the said heat exchangers.3. An apparatus of claim 2 wherein said absorber includes a heat exchanger coil in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said heat exchanger coil and is at least partially vaporized therein to cool said absorber, and wherein said refrigerant loop includes piping for directing vaporized refrigerant from said absorber heat exchanger coil and from said generator assembly to said condenser.4. An apparatus of claim 3 including a rectifier and a cooling coil therein in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said cooling coil and is heated and/or at least partially vaporized therein to cool said rectifier, and wherein said refrigerant loop includes piping for directing heated and/or vaporized refrigerant from said cooling coil to said condenser.5. An apparatus of claim 1,2,3 or4 wherein said absorber assembly includes an absorber, an absorber heat exchanger and a generator/absorber heat exchanger and wherein said absorption fluid loop includes one or more conduits for directing ammonia-rich absorption fluid in the absorber assembly from the absorber to the absorber heat exchanger and the generator/absorber heat exchanger.6. An apparatus of claim 1,2,3 or4 wherein a first valve has a pressure port exposed to the temperature-sensing bulb pressure and wherein said first side of the movable member is exposed to said pressure port, an inlet port communicating with said generator and an outlet port communicating with said absorber.7. An apparatus of claim 5 wherein a first valve has a pressure port exposed to the temperature-sensing bulb pressure and wherein said first side of the movable member is exposed to said pressure port, an inlet port communicating with said generator and an outlet port communicating with said absorber.8. An apparatus of claim 1 having a bulb charge composition comprising FeCl2.2/6(NH3).9. An apparatus of claim 1 including providing a bulb charge composition comprising BaCl2.1/2(H2O).10. An apparatus method of claim 1 including providing a bulb charge composition comprising a mixture of ammonia and water.11. An apparatus of claim 10 wherein the concentra tion of ammonia is between about 1% and about 20%, by weight, of said bulb charge composition.12. An aqua-ammonia absorption cooling and/or heating apparatus comprising: an absorber assembly, a generator assembly, a condenser, an evaporator, a refrigerant loop for directing refrigerant between said absorber assembly, generator assembly, condenser and evaporator, an absorption fluid loop for directing absorption fluid between said absorber assembly and said generator assembly, said absorption fluid loop including first piping for directing ammonia-rich absorption fluid from the absorber assembly to the generator assembly and second piping for directing ammonia-weak absorption fluid from the generator assembly to the absorber assembly, a valve assembly comprising one or more valves cooperating with the second piping for controlling the flow rate of weak absorption fluid therein, and a sensing device for sensing concentration of the ammonia-weak absorption fluid or a property or condition correlated thereto and operatively connected to said valve assembly for operating said one or more valves in response to the sensed concentration or correlated property or condition of the ammonia-weak absorption fluid. 13. An apparatus of claim 12 wherein said absorber assembly includes an absorber, an absorber heat exchanger and a generator/absorber heat exchanger and wherein said absorption fluid loop includes one or more conduits for directing ammonia-rich absorption fluid in the absorber assembly from the absorber to the absorber heat exchanger and the generator/absorber heat exchanger.14. An apparatus of claim 13 wherein said absorber includes a heat exchanger coil in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said heat exchanger coil and is at least partially vaporized therein to cool said absorber, and wherein said refrigerant loop includes piping for directing vaporized refrigerant from said absorber heat exchanger coil and from said generator assembly to said condenser.15. An apparatus of claim 14 including a rectifier and a cooling coil therein in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said cooling coil and is heated and/or at least partially vaporized therein to cool said rectifier, and wherein said refrigerant loop includes piping for directing heated and/or vaporized refrigerant from said cooling coil to said condenser.16. An apparatus of claim 12 wherein said second piping includes one or more flow restriction devices in series or in parallel with said one or more valves.17. An apparatus of claim 16 wherein said second piping includes a flow splitter and a plurality of conduits communicating therewith for directing portions of ammonia-weak absorption fluid to a said valve and said flow restriction device, respectively.18. An apparatus of claim 16 wherein said second piping includes a flow splitter and first and second conduits communicating therewith, and a valve and/or a flow restriction device along said first and second conduits, and wherein said sensing device is operatively connected to at least one of said valves.19. An apparatus of claim 12 or17 wherein said valve assembly includes one or more valve control components operatively connected to said sensing device.20. An apparatus of claim 12 or17 including a controller having a controller function component for controlling operation of said one or more valves, and wherein said sensing device is operatively connected to said controller or controller function component.21. An aqua-ammonia absorption cooling and/or heating apparatus comprising: an absorber assembly, a generator assembly, a condenser, an evaporator, a refrigerant loop for directing refrigerant between said absorber assembly, generator assembly, condenser and evaporator, an absorption fluid loop for directing absorption fluid between said absorber assembly and said generator assembly, said absorption fluid l oop including first piping for directing ammonia-rich absorption fluid from the absorber assembly to the generator assembly and second piping having one or more flow restriction devices for directing ammonia-weak absorption fluid from the generator assembly to the absorber assembly, a sensing device for sensing a condition and a valve assembly communicating therewith comprising one or more valves cooperating with the second piping and said flow restriction devices for controlling the flow rate of weak absorption fluid therein in response to a sensed condition. 22. An apparatus of claim 21 wherein said absorber includes a heat exchanger coil in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said heat exchanger coil and is at least partially vaporized therein to cool said absorber, and wherein said refrigerant loop includes piping for directing vaporized refrigerant from said absorber heat exchanger coil and from said generator assembly to said condenser.23. An apparatus of claim 22 including a rectifier and a cooling coil therein in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said cooling coil and is heated and/or at least partially vaporized therein to cool said rectifier, and wherein said refrigerant loop includes piping for directing heated and/or vaporized refrigerant from said cooling coil to said condenser.24. An apparatus of claim 21,22 or23 wherein said absorber assembly includes an absorber, an absorber heat exchanger and a generator/absorber heat exchanger and wherein said absorption fluid loop includes one or more conduits for directing ammonia-rich absorption fluid in the absorber assembly from the absorber to the absorber heat exchanger and the generator/absorber heat exchanger.25. An apparatus of claim 21 wherein said second piping includes one or more flow restriction devices in series or in parallel with one or more of said valves.26. An apparatus of claim 25 wherein said second piping includes a flow splitter and a plurality of conduits communicating therewith for directing portions of ammonia-weak absorption fluid to a said valve and said flow restriction device, respectively.27. An apparatus of claim 21 wherein said valve assembly includes a valve control component operatively communicating with a control device.28. An apparatus of claim 27 wherein said second piping includes a flow splitter and first and second conduits communicating therewith, and a valve and/or a flow restriction device along said first and second conduits, and wherein said control device is operatively connected to at least one of said valves.29. An apparatus of claim 21 including a sensing device operatively communicating with said valve for opening and/or closing the valve in response to a sensed condition.30. An apparatus of claim 29 wherein said sensed condition comprises a load related condition.31. An apparatus of claim 30 wherein said load related condition comprises chilled water supply and/or return water temperature.32. An apparatus of claim 29 wherein said sensed condition comprises burner speed.33. An apparatus of claim 29 wherein said sensed condition comprises absorption fluid pressure, temperature and/or concentration.34. An apparatus of claim 29 wherein said sensing device is in sensible contact with ammonia-weak absorption fluid.35. An apparatus of claim 29 including a controller or microprocessor operatively communicating with said valve and said sensing device for opening and/or closing said valve.36. An apparatus of claim 35 wherein said sensing device senses a load condition.37. An apparatus of claim 35 wherein said valve is operated by pulse-width modulation control.38. An apparatus of claim 29 wherein said absorber includes a heat exchanger coil in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said heat exchanger coil and is at least partially vaporized therein to cool said abso rber, and wherein said refrigerant loop includes piping for directing vaporized refrigerant from said absorber heat exchanger coil and from said generator assembly to said condenser.39. An apparatus of claim 38 including a rectifier and a cooling coil therein in fluid communication with said refrigerant loop whereby condensed refrigerant is directed to said cooling coil and is heated and/or at least partially vaporized therein to cool said rectifier, and wherein said refrigerant loop includes piping for directing heated and/or vaporized refrigerant from said cooling coil to said condenser.40. An apparatus of claim 29 wherein said absorber assembly includes an absorber, an absorber heat exchanger and a generator/absorber heat exchanger and wherein said absorption fluid loop includes one or more conduits for directing ammonia-rich absorption fluid in the absorber assembly from the absorber to the absorber heat exchanger and the generator/absorber heat exchanger.41. An apparatus of claim 21 including electronic control apparatus operatively connected to said one or more valves and one or more components for sensing building load and/or one or more parameters thereof operatively connected to said electronic control apparatus for controlling the operation of said one or more valves in response to load and/or one or more load parameters.42. An apparatus of claim 41 wherein said one or more load parameters comprise chilled water or return temperature.43. An apparatus of claim 1,12 or21 comprising a temperature-sensing bulb in thermal contact with said evaporator at or near the evaporator outlet and a refrigerant control valve cooperating with said refrigerant piping, wherein said refrigerant control valve includes a pressure port exposed to the temperature-sensing bulb pressure, and a movable member exposed to said pressure port and responsive to bulb pressure for operating said valve and for controlling refrigerant flow therethrough in response to temperature sensed by the temperature-sensing bulb, said movable member having a first side exposed to temperature-sensing bulb pressure and a second side exposed to evaporator pressure, whereby said movable member causes the refrigerant control valve to operate in response to the pressure differential between the temperature-sensing bulb and the evaporator, and wherein said temperature-sensing bulb is located above said movable member.44. An apparatus of claim 43 wherein said refrigerant control valve comprises a pulsed operation control valve comprising: an inlet port in communication with said condenser having an inlet flow area for receiving condensed refrigerant, and a valve for opening and closing said inlet port; an outlet port having an outlet flow area and communicating with said evaporator for directing liquid refrigerant thereto; a valve cavity between said inlet port and said outlet port and in open communication therewith; said valve being responsive to pressure within said valve cavity for operating the valve and controlling the opening and closing of said inlet port, and wherein higher pressure therein biases said valve to close said inlet port and lower pressure therein biases valve to open said inlet port; and said inlet flow area being at least twice the size of said outlet flow area whereby opening said inlet port provides for rapid pressure buildup in said cavity and rapid closure thereof after each opening. 45. A method of improving efficiency of an aqua-ammonia absorption heating and/or cooling system in which ammonia-weak absorption fluid is directed through piping from the generator assembly to the absorber assembly comprising providing one or more valves cooperating with the piping capable of controlling the flow of fluid therethrough, and a temperature-sensing device in thermal contact with the ammonia-weak absorption fluid, and operating said one or more valves in response to the temperature of said ammonia-weak absorption fluid. 46. A method of cla im 45 comprising monitoring the ammonia-weak absorption solution temperature in the generator assembly where the solution is at or near its bubble-point temperature.47. A method of claim 45 or46 wherein said valve is operated by a movable member, wherein said temperature-sensing device is a temperature-sensing bulb, and wherein a first side of said movable member is exposed to bulb pressure and a second side thereof is exposed to generator pressure or ammonia-weak absorption fluid at or near generator pressure, and comprising controlling the flow of said ammonia-weak absorption fluid by opening and closing said valve in response to pressure differential between bulb pressure and generator pressure.48. A method of claim 47 including providing a bulb charge composition comprising FeCl2.2/6(NH3).49. A method of claim 47 including providing a bulb charge composition comprising BaCl2.1/2(H2O).50. A method of claim 47 including providing a bulb charge composition comprising a mixture of ammonia and water.51. A method of claim 50 wherein the concentration of ammonia in a said bulb charge composition is between about 1% and about 20% by weight.52. In an aqua-ammonia absorption heating and/or cooling system in which ammonia-weak absorption fluid is directed from the generator to the absorber a method of maintaining the concentration of ammonia in the ammonia-weak absorption fluid comprising controlling the flow rate of said ammonia-weak absorption fluid directed from said generator to said absorber. 53. A method of claim 52 including sensing the temperature, pressure or concentration of said ammonia-weak absorption fluid in said generator and controlling said flow rate in response thereto.