Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
159 words
In a solar heating system wherein a mixture of refrigerant in liquid and vapor form is circulated through a solar collector which takes heat from the atmosphere to convert the refrigerant to a superheated vapor preparatory to delivering it to a compressor, and wherein means responsive to the temperature of the superheated vapor leaving the collector is employed to control the amount of the mixture admitted to the latter, the improved method for reducing any excess superheat contained in the superheated vapors which comprises: sensing the degree of superheat contained in the superheated vapors entering the compressor, using any excess of superheat detected above a preselected maximum as an input operative to actuate means connected to bypass the refrigerant mixture around the collector and mix same directly with the overheated vapors, and employing the refrigerant mixture thus bypassed to cool down the overheated vapors to the preselected maximum temperature chosen for the superheated vapors being fed to the compressor.
Claim 2
Dependent Claim
159 words
In a solar heating system wherein a mixture of refrigerant in liquid and vapor form is circulated through a solar collector which takes heat from the atmosphere to convert the refrigerant to a superheated vapor preparatory to delivering it to a compressor, and wherein means responsive to the temperature of the superheated vapor leaving the collector is employed to control the amount of the mixture admitted to the latter, the improved method for reducing any excess superheat contained in the superheated vapors which comprises: sensing the degree of superheat contained in the superheated vapors entering the compressor, using any excess of superheat detected above a preselected maximum as an input operative to actuate means connected to bypass the refrigerant mixture around the collector and mix same directly with the overheated vapors, and employing the refrigerant mixture thus bypassed to cool down the overheated vapors to the preselected maximum temperature chosen for the superheated vapors being fed to the compressor.
Claim 3
Dependent Claim
32 words
The improved method as set forth in claim 1 wherein none of the refrigerant mixture is bypassed around the collector before the means controlling delivery thereof to said collector is fully open.
Claim 4
Dependent Claim
35 words
The improved method as set forth in claim 1 wherein the preselected maximum superheated vapor temperature is set at a level higher than that chosen to control admission of the refrigerant mixture to the collectors.
Claim 5
Dependent Claim
26 words
The improved method as set forth in claim 1 wherein the preselected maximum amount of superheat permitted in the vapor is between approximately 15° and 30°F.
Claim 6
Dependent Claim
47 words
The improved method as set forth in claim 1 wherein the preselected maximum temperature of the superheated vapor is set between approximately 5° and approximately 20° F. higher than the chosen temperature at which superheated vapor activates the means for admitting the refrigerant mixture to the collector.
Claim 7
Dependent Claim
172 words
In a solar heating system having a solar collector wherein heat is taken from the atmosphere to convert a refrigerant mixture in liquid and vapor form to a superheated vapor for delivery to a compressor, and wherein a first thermostatic expansion valve responsive to the temperature of the superheated vapor leaving the collector is connected to control the amount of refrigerant mixture admitted to the collector, the improved means for limiting the amount of superheat contained in the vapor fed to the compressor which comprises: a bypass line connected to take the refrigerant mixture following condensation thereof out at a point upstream of the first thermostatic expansion valve and convey same around the collector to a point where it is mixed with the superheated vapor upstream of the compressor; and a second thermostatic expansion valve operative in response to a rise in temperature of the superheated vapor above a preselected maximum to bypass that portion of the refrigerant mixture required to maintain said vapor at the preselected temperature upon being mixed therewith.
Claim 8
Dependent Claim
172 words
In a solar heating system having a solar collector wherein heat is taken from the atmosphere to convert a refrigerant mixture in liquid and vapor form to a superheated vapor for delivery to a compressor, and wherein a first thermostatic expansion valve responsive to the temperature of the superheated vapor leaving the collector is connected to control the amount of refrigerant mixture admitted to the collector, the improved means for limiting the amount of superheat contained in the vapor fed to the compressor which comprises: a bypass line connected to take the refrigerant mixture following condensation thereof out at a point upstream of the first thermostatic expansion valve and convey same around the collector to a point where it is mixed with the superheated vapor upstream of the compressor; and a second thermostatic expansion valve operative in response to a rise in temperature of the superheated vapor above a preselected maximum to bypass that portion of the refrigerant mixture required to maintain said vapor at the preselected temperature upon being mixed therewith.
Claim 9
Dependent Claim
36 words
The improved solar heating system as set forth in claim 6 wherein the second thermostatic expansion valve becomes operative to bypass the refrigerant mixture only after the first of said thermostatic expansion valves is fully open.
Claim 10
Dependent Claim
52 words
The improved solar system as set forth in claim 6 wherein said second thermostatic expansion valve becomes operative to bypass the refrigerant mixture at a superheated vapor temperature between approximately 5° and approximately 20° F. above the temperature of the superheated vapor at which said first thermostatic expansion valve is fully open.
Claim 11
Dependent Claim
41 words
The improved solar collection system as set forth in claim 6 wherein the second thermostatic expansion valve becomes operative to bypass the refrigerant mixture when the superheated vapor contains between approximately 15 and 30 degrees of superheat on the Fahrenheit scale.