Methods and apparatus for linearized temperature control of commercial refrigeration systems
View Patent ↗Methods, systems, and apparatus for linearizing control of a commercial refrigeration system. In an embodiment of the invention, a controller is configured to receive a non-linear sensed suction pressure and convert the suction pressure to a linear temperature equivalent. The linear temperature equivalent is used by the controller to achieve efficient system operation over an entire range of operating temperatures.
1. A controller for a commercial refrigeration system for cooling a plurality of spaces, two or more of the plurality of spaces cooled to a respective temperature, the controller linearly operable over a temperature range, the controller comprising:
a sensor configured to detect a suction pressure;
a converter configured to convert the suction pressure to an equivalent temperature; and
a proportional-integral-derivative controller configured to receive the equivalent temperature and a temperature set-point representing a desired temperature for at least one of the plurality of spaces as control variables, and a set of static control parameters, and to generate an output, the output controlling a plurality of compressors and providing linear control over the temperature range,
wherein the suction pressure is not linear over the temperature range, and the static control parameters remain constant over the temperature range.
2. The controller of claim 1 wherein the equivalent temperature is a function of the sensed suction pressure and a type of refrigerant.
3. The controller of claim 1 wherein the equivalent temperature is determined by a calculation.
4. The controller of claim 1 wherein the equivalent temperature is determined by accessing a lookup table.
5. The controller of claim 1 wherein the converter is configured to convert a pressure set-point to the temperature set-point.
6. A linear control method for a commercial refrigeration system, the method comprising:
providing a set of control parameters to a controller, the set of control parameters static over the controller's range of operation;
providing a temperature set-point as a first control variable to the controller;
sensing a suction pressure, the suction pressure being non-linear over the controller's range of operation;
determining a temperature equivalent to the sensed suction pressure;
providing the temperature equivalent as a second control variable to the controller; and
adjusting an output of the controller based on a magnitude of a difference between the temperature set-point and the temperature equivalent,
wherein the adjusted output of the controller modifies operation of at least one of a plurality of compressors in the commercial refrigeration system.
7. The method of claim 6 wherein the temperature equivalent is a function of the sensed suction pressure and a type of refrigerant.
8. The method of claim 6 wherein the temperature equivalent is determined by a calculation.
9. The method of claim 6 wherein the temperature equivalent is determined by accessing a lookup table.
10. The method of claim 6 wherein the controller is a proportional-integral-derivative controller.
11. The method of claim 6 and further comprising converting a pressure set-point to the temperature set-point.
12. The method of claim 6 wherein the adjusted output of the controller modifies operation of a plurality of compressors in the commercial refrigeration system.