SYSTEM OR METHOD FOR MEASURING THE PHASE OF AMMONIA IN A COOLING SYSTEM

Abstract

A system or a method for performing capacitive sensing of humidity/liquid, primarily in conductive or non-conductive liquid/gas mixtures, having a control unit and at least first and second sensor electrodes, the capacity between the first and the second electrodes being measured,. To measure humidity/liquid in a circulating gas/liquid mixture at least one of the sensor electrodes is formed as a tube which is placed in the liquid/gas mixture. Based on the capacitive measurements, a calculation of at least one dataset for control of a second system is performed. The tube can be more or less filled up with liquid or gas and the capacity can be measured as it depends on the content around or inside the tube, and if a dry gas is there will be one value of capacity and in a situation where the gas is being replaced by liquid, the capacity value will change rapidly.

Claims

1. A refrigeration system comprising at least one compressor which compressor delivers compressed refrigerant gas to at least one condenser, which condenser delivers liquid refrigerant to at least one flow restriction, from which flow restriction, low pressure refrigerant flows to at least one evaporator, from which evaporated refrigerant flows back to the compressor, which system comprises at least one sensor for detecting liquid refrigerant in the suction gas which sensor is connected to a control unit, which control unit performs control of the refrigeration system, which sensor is formed as at least one capacitive sensor, which capacitive sensor comprises at least a first and a second sensor electrode, which capacity sensor at least measures the capacity between at least the first and at least the second electrodes, where at least one of the sensor electrodes are formed as a tube, whereby the tubes measure the liquid/gas content of the suction gas between evaporator and compressor, which control system based on capacitive measurements obtained by the capacity sensor performs a calculation of at least one dataset for control of the refrigeration system, wherein the system is adapted to perform control of an expansion valve, which expansion valve is adapted to control a liquid refrigerant inlet to the at least one evaporator and thereby control of the overheating of the at least one evaporator.

2. A refrigeration system according to claim 1, whereby the first and second sensor electrodes are formed mostly coaxial, forming a first outer electrode tube, which first outer electrode tube comprises at least one second inner electrode tube.

3. A refrigeration system according to claim 2, whereby the first outer sensor tube is part of a tube in a cooling system , which second inner tube is placed inside the outer tube and electric isolated from the outer tube, which system measures the capacity between the first outer tube and at least one second inner tube.

4. A refrigeration system according to claim 3, whereby the outer tube is part of a tube connecting the evaporator with the suction inlet of the compressor for indicating liquid in the suction gas.

5. Method for indicating liquid refrigerant in a cooling system, which method comprises at least the following steps: a. place at least a first measuring electrode inside a cooling circuit, b. connect the electrode to a measuring circuit, c. perform measurement of the capacity between electrode and a reference, d. transmit the measured capacity to a control system, e. perform control of the cooling system based on the measured capacity, f. the capacity is measure between an inner tube and an outer tube, g. perform measurement of liquid in refrigeration gas flowing in the outer and inner tube towards a compressor. h. perform control of the cooling system based of the measurement of liquid refrigerant in the suction gas towards one or more compressors. j. perform control of an expansion valve, which expansion valve is adapted to control liquid refrigerant inlet to the evaporator. k. perform control of the overheating of the evaporator.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0016] FIG. 1 shows a schematic view of a cooling system, where

[0017] FIG. 2 shows a section of a suction tube,

[0018] FIG. 3 shows a level indicator,

[0019] FIG. 4 show a second section of a suction tube,

[0020] FIGS. 5a-5d show four possible embodiments for cooling systems, and

[0021] FIG. 6 show the relation between density of refrigerant and the sensor level.

DETAILED DESCRIPTION OF THE INVENTION

[0022] FIG. 1 shows a cooling system 2 which cooling system comprises a cooling media for circulating in the system. Sensors 6.8 are placed in the gas return line 20 which is leading from an evaporator 24 through the first sensor 6.8 towards the second sensor 6.8 further through the suction line 26 to the compressor 28. The two sensors 6.8 are both connected to the control unit 10. From the compressor 28, the compressed refrigerant is sent to a not shown condenser where liquid refrigerant 4 is received and sent to the expansion valve 30. From the expansion valve 30 leads a tube 32 into the evaporator 24.

[0023] In operation the first of the sensors 6.8 can measure the content of humidity in the gas in the line 20 leaving the evaporator. This measurement can be used for controlling the expansion valve. As long as the gas leaving the tube 20 is dry, the expansion valve can remain open. As soon as liquid is indicated in the line 20, the expansion valve can be reduced in its opening, so further evaporation takes place. Hereby it is possible to operate the evaporator with a very limited superheating. Furthermore, before the gas enters the compressor further one detector 6.8 is indicated as 34. This sensor 6.8 and 34 is used as a liquid alarm. If liquid is detected, the compressor might be shut down or the speed is reduced.

[0024] FIG. 2 shows a sectional view of a tube section, for example the tube 20 at the FIG. 1. The detector is made inside the tube 20 where the detector 6 and 12 are all referring to the same component. Inside the tube 20 is indicated an inner tube which is indicated as 8, 14 and 22. The inner tube 22 is kept in place by fixtures 40 where a conducting screw 42 connects the inner tube 22 electrically and where the screw 44 is an isolating screw that isolated the inner tube towards the outer tube 20. In operation it is possible to measure the capacity between the inner tube and the outer tube. Since the flow of liquid or gas is passing through both the tubes, there is nearly no flow restriction. However, even small amounts of liquid in the circulating gas can be detected, because even small drops of liquid have a relatively high influence on the capacity that is measured between the two tubes. Therefore it is possible by the capacity measurement to indicate liquid particles in gas, and therefore adjustment of a cooling system can be performed immediately.

[0025] FIG. 3 shows a system 102 for level detection. The level detector comprises an outer tube 120 and an inner tube 122. The inner tube comprises a first section 124 and the second section 126. The two sections are separated by isolation means 128. The inner tube 122 is placed inside a partly open tube 132. The inner tube and the outer tube are placed in relation to a screw 134 and a housing 134. A measuring system 140 is connected to the lines 142, 144. The line 142 is connected to the tube section 126 and the second line 144 is connected to the tube section 124.

[0026] In operation, a reference can be achieved if the section 124 is submerged in the liquid. Thereby a reference value can be calculated. The tube section 126 can hereafter perform an indication of the level of liquid around the tube. In that way it is possible to indicate the level of, for example, refrigerant in one or another tank as part of a refrigeration system, or it is possible to indicate the level of oil in a refrigeration system. The system at FIG. 3 can be a highly effective oil indicator in refrigeration systems. The system could be placed, for example, in a submerged evaporator and there it could indicate the oil level in the evaporator. Hereby it is possible to start a pump or indicate that manual opening of a valve to tap the oil is necessary. In many modern systems the oil return is performed automatically by pumping systems.

[0027] FIG. 4 shows a sectional view of a tube section, for example the tube 220 at the FIG. 4. The detector 206 is made inside the tube 220 where the detector 206 and 212 are all referring to the same component. Inside the tube 220 is indicated an inner tube 222. The inner tube 222 is kept in place by fixtures 240 where a conducting screw 242 connects the inner tube 222 electrically and where the screw 244 is an isolating screw that isolated the inner tube towards the outer tube 220. The detector 206 further comprises a second inner tube 250, which second inner tube 250 is fixed to the outer tube 220 by conductive fixtures 252.

[0028] In operation, it is possible to measure the capacity between the inner tube and the outer tube and also between the first inner tube and the second inner tube. Hereby is the actual electric capacity increased and more accurate measurement can be achieved.

[0029] FIGS. 5a-5d shows a cooling system which is divided into four different subsystems where only a compressor 328, a condenser 340, and a receiver 342 are common.

[0030] FIG. 5a shows a system 302a which is by a high pressure line 304 connected to the receiver 342. This line 304 is connected to an expansion valve 330a and further through a connection line 332a to an evaporator 324a. A suction line 320a is connected to a sensor 306, 308a which is electrically connected to a control unit 310a. A suction line 326 is connects the refrigerant to the suction side of a compressor 328.

[0031] In operation, the sensor 306,308a will measure the suction gas and indicate any liquid drops that are carried in the gas. The control unit 31a controls the expansion valve 330a so by indicating any liquid drop in the sensor 306, 308, the expansion valve is more or less closed, or at least the flow though the expansion valve 330a is reduced. In this way it is achieved that the suction gas that reaches the compressor 328 is absolutely dry and free from any liquid droplets.

[0032] In FIG. 5b the expansion valve 330b is also connected to the line 304 from the receiver 342. The expansion valve 330b is delivering liquid refrigerant to a tank 322 from where a line 332b is connected to the evaporator 324b. The evaporator is connected by a line 320b into the tank 322. From the tank 322 there is a suction line connected to the sensor 306, 308b. The sensor 306,308b is connected to a control unit 310b which is further connected to a liquid level indicator 323. The control unit 310b is controlling the flow through the expansion valve 330b so that the liquid level in the tank 322 can be controlled. In this way the liquid level can be under control according to two different parameters. One parameter is the liquid level, the other is the existence of liquid drops in the detector 306,308b. In this way it can be achieved that the will always be sufficient liquid refrigerant for the evaporator 324b, and there will always be control of the suction gas delivered to the compressor. The use of the tank 322 has the advantage that the evaporator 324 can be fully submerged. The tank 322 operates as a liquid separator.

[0033] FIG. 5c shows a subsystem 302c. Again the line 304 is connected to the expansion valve 330c from which expansion valve 330c a line 332c connects towards the evaporator 324c. The outlet of the evaporator 324c is via a line 320c connected to a sensor 306, 308c. The outlet of this sensor is connected to a separation tank 322. From this separation tank evaporated refrigerant is sucked to the suction side of the compressor 328. Liquid refrigerant is collected by a pump 325 which pump outlet is connected to the pressure line 304 that supplies liquid refrigerant towards the expansion valve 330c. By means of the control unit 310c the sensor 306,308c controls the expansion valve 330c and the pump 325.

[0034] Hereby a total control of the evaporator 324c can be achieved. At the same time it is achieved that no liquid droplets will be contained in the suction gas that reaches the compressor 328.

[0035] FIG. 5d shows a system 302d which, like the ones previously described, also receives liquid high-pressure refrigerant over the line 304. The expansion valve 330d is further connected by a line 332d to a submerged evaporator 324d. A line 320d is connecting sensor 306, 308d to the suction line 326 connected to the suction side of the compressor 328. The sensor 306,308d is connected to a control unit 310d which controls the expansion valve 330d. In this way it is possible to close or reduce the flow through the expansion valve when droplets of liquid refrigerant are measured by the sensor 306,308d. In this way it can be ensured that the suction line towards the compressor only carries dry gas and the evaporator is completely filled with liquid refrigerant.

[0036] A system as shown in FIG. 5 could be used for different types of refrigerant where one possible refrigerant can be ammonia NH3.

[0037] FIG. 6 shows a coordinate system which vertical axes indicate the density of the refrigerant flowing through a sensor, and the horizontal axis shows the signal level that can be indicated. The curve that is shown indicates that a relatively low signal level is achieved if superheated refrigerant is passing the sensor. But, as the refrigerant starts to be saturated there is a rapid increase in the signal level. That increase in signal level continues until the refrigerant phase becomes totally liquid. Indicated at FIG. 6 is the control P-band where the refrigeration system mostly is operating where there is the area around the superheated and the saturated phase.

[0038] Operating in the said P-band, it is possible to avoid liquid refrigerant in the suction line towards the compressor and in that way totally avoid compressor hamming. A further effect that is achieved is that the cooling system can operate very near the saturated system whereby the effectivity of evaporators is increasing.

[0039] It is also possible to use the capacitive sensors to control humidity content in intake air for combustions processes. By using the humidity content as input for a computer system that controls the combustion process it is possible to reduce pollution and reduce fuel consumption. The system can be used for control of engines in ships, cars or airplanes.