IPC분류정보
국가/구분 |
United States(US) Patent
등록
|
국제특허분류(IPC7판) |
|
출원번호 |
US-0394412
(2009-02-27)
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등록번호 |
US-8375734
(2013-02-19)
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발명자
/ 주소 |
- Hall, David L.
- Scoville, James
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출원인 / 주소 |
- Electrolux Home Products, Inc.
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인용정보 |
피인용 횟수 :
2 인용 특허 :
14 |
초록
▼
A refrigeration system is provided with an ice maker chamber within a fresh food compartment. The refrigeration system includes a refrigeration path and an ice maker path. The ice maker path includes an electronic expansion valve for controlling the refrigerant entering an ice maker evaporator and a
A refrigeration system is provided with an ice maker chamber within a fresh food compartment. The refrigeration system includes a refrigeration path and an ice maker path. The ice maker path includes an electronic expansion valve for controlling the refrigerant entering an ice maker evaporator and an evaporator pressure regulator. Controlling the refrigeration system includes the steps of sensing a first refrigerant temperature at an exit of the ice maker evaporator and controlling a first control of the electronic expansion valve until the temperature reaches a temperature target. The method of controlling can further include comparing a slope of the temperature to at least one of a minimum, a target, or a maximum setting to adjust the control. Subsequently, a second control for the electronic expansion valve can be repeatedly adjusted by evaluating the first refrigerant temperature and the slope.
대표청구항
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1. A method of controlling a refrigeration system comprising the steps of: sensing a first refrigerant temperature at an exit of an evaporator over a first period of time;providing a first valve located at a point before the inlet of the evaporator;repeatedly adjusting a first control for a variable
1. A method of controlling a refrigeration system comprising the steps of: sensing a first refrigerant temperature at an exit of an evaporator over a first period of time;providing a first valve located at a point before the inlet of the evaporator;repeatedly adjusting a first control for a variable degree of opening of the first valve by using the first refrigerant temperature to operate an initial refrigerant loading of the evaporator;comparing the first refrigerant temperature to the first period of time to calculate a first slope;comparing the first slope to at least one of a first minimum slope setting, a first target slope setting, or a first maximum slope setting to repeatedly adjust the first control of the first valve;wherein the first valve operates at the first control until the refrigerant at the exit of the evaporator reaches a first refrigerant temperature target; andrepeatedly adjusting a second control for a variable degree of opening of the first valve of the opening of the first valve between a fully closed position and a fully open position for operating a post-initial refrigerant loading state of the evaporator by evaluating the first refrigerant temperature and the first slope subsequent to the refrigerant at the exit of the evaporator reaching the first refrigerant temperature target and the initial refrigerant loading being completed. 2. The method of claim 1, further comprising the step of: activating a heating element when a release of ice produced by the evaporator is desired. 3. The method of claim 1, further comprising the steps of: not adjusting the second control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target, when the first slope is less than a second target slope setting, and when the first refrigerant temperature is within a range between a first constant and a second constant. 4. The method of claim 3, further comprising the steps of: designating a first set of values for the first constant and the second constant if the first valve is at a range of closed positions;designating a second set of values for the first constant and the second constant if the first valve is at a range of intermediate positions; anddesignating a third set of values for the first constant and the second constant if the first valve is at a range of open positions. 5. The method of claim 3, wherein: the first constant is equal to approximately negative 19° C. and the second constant is equal to approximately negative 12° C. 6. The method of claim 1, further comprising the step of: decreasing the variable degree of opening of the second control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target, when the first slope is less than a second target slope setting, and when the first refrigerant temperature is not within a range between a first constant and a second constant. 7. The method of claim 1, further comprising the step of: increasing the variable degree of opening of the second control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target and when the first slope is greater than a second target slope setting. 8. The method of claim 1, further comprising the step of: running a reload subroutine that repeatedly increases the variable degree of opening of the second control;wherein the reload subroutine is activated when the first refrigerant temperature is less than the first refrigerant temperature target and when the first slope is greater than a second target slope setting;wherein the reload subroutine is deactivated when the first slope is less than a fourth constant;wherein the second control is decreased upon deactivation of the reload subroutine. 9. The method of claim 1, further comprising the step of: increasing the variable degree of opening of the second control of the first valve during the post-initial refrigerant loading state of the evaporator when the first refrigerant temperature is greater than the first refrigerant temperature target. 10. The method of claim 1, further comprising the step of: running a reload subroutine that repeatedly increases the variable degree of opening of the second control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target; andwherein the reload subroutine is deactivated when the first slope is less than a fourth constant;wherein the second control is decreased upon deactivation of the reload subroutine. 11. The method of claim 1, further comprising the steps of: running a reload subroutine that repeatedly increases the variable degree of opening of the second control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target when the first slope is less than a second target slope setting, and when the first refrigerant temperature is less than a third constant;designating a first value for the third constant if the first valve is at a range of closed positions;designating a second value for the third constant if the first valve is at a range of intermediate positions; anddesignating a third value for the third constant if the first valve is at a range of open positions. 12. The method of claim 11, wherein the third constant is equal to approximately negative 1° C. 13. The method of claim 1, further comprising the steps of: increasing the variable degree of opening of the second control of the first valve by a first amount when the first refrigerant temperature is greater than the first refrigerant temperature target, the first slope is greater than a second target slope setting and when the first refrigerant temperature is greater than a third constant; andincreasing the variable degree of opening of the second control of the first valve by a second amount when the first refrigerant temperature is greater than the first refrigerant temperature target, the first slope is greater than the second target slope setting, and when the first refrigerant temperature is less than the third constant. 14. The method of claim 1, further comprising the step of: running a reload subroutine that repeatedly increases the variable degree of opening of the second control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target, when the first slope is greater than a second target slope setting;wherein the reload subroutine is deactivated when the first slope is less than fourth constant;wherein the variable degree of opening of the second control is decreased upon deactivation of the reload subroutine. 15. The method according to claim 1, wherein the evaporator is a storage evaporator configured to control a temperature within an ice chamber; andwherein the evaporator is located downstream from an ice maker evaporator that is configured to furnish a cooling effect sufficient to freeze water. 16. A method of controlling a refrigeration system comprising the steps of: sensing a first refrigerant temperature at an exit of an evaporator over a first period of time wherein the evaporator is configured to furnish a cooling effect sufficient to freeze water;providing a first valve located at a point before the inlet of the evaporator;comparing the first refrigerant temperature to the first period of time to calculate a first slope; andrepeatedly adjusting a control for a variable degree of opening of the first valve between a fully closed position and a fully open position for operating a post-initial refrigerant loading state of the evaporator by evaluating the first refrigerant temperature and the first slope subsequent to the refrigerant at the exit of the evaporator reaching a first refrigerant temperature target. 17. The method of claim 16, further comprising the step of: not adjusting the control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target, when the first slope is less than a second target slope setting, and when the first refrigerant temperature is within a range between a first constant and a second constant. 18. The method of claim 16, further comprising the step of: decreasing the variable degree of opening of the control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target, when the first slope is less than a second target slope setting, and when the first refrigerant temperature is not within a range between a first constant and a second constant. 19. The method of claim 16, further comprising the step of: increasing the variable degree of opening of the control of the first valve when the first refrigerant temperature is less than the first refrigerant temperature target and when the first slope is greater than a second target slope setting. 20. The method of claim 16, further comprising the step of: running a reload subroutine that repeatedly increases the variable degree of opening of the control;wherein the reload subroutine is activated when the first refrigerant temperature is less than the first refrigerant temperature target, when the first slope is greater than a second target slope setting;wherein the reload subroutine is deactivated when the first slope is less than a fourth constant;wherein the control is decreased upon deactivation of the reload subroutine. 21. The method of claim 16, further comprising the step of: increasing the variable degree of opening of the control of the first valve during the post-initial refrigerant loading state of the evaporator when the first refrigerant temperature is greater than the first refrigerant temperature target. 22. The method of claim 16, further comprising the step of: running a reload subroutine that repeatedly increases the control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target when the first slope is less than a second target slope setting, and when the first refrigerant temperature is less than a third constant; andwherein the reload subroutine is deactivated when the first slope is less than a fourth constant;wherein the control is decreased upon deactivation of the reload subroutine. 23. The method of claim 16, further comprising the steps of: increasing the variable degree of opening of the control of the first valve by a first amount when the first refrigerant temperature is greater than the first refrigerant temperature target, the first slope is greater than a second target slope setting and when the first refrigerant temperature is greater than a third constant; andincreasing the variable degree of opening of the control of the first valve by a second amount when the first refrigerant temperature is greater than the first refrigerant temperature target, when the first slope is greater than the second target slope setting, and when the first refrigerant temperature is less than the third constant. 24. The method of claim 16, further comprising the step of: running a reload subroutine that repeatedly increases the variable degree of opening of the control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target, when the first slope is greater than a second target slope setting;wherein the reload subroutine is deactivated when the first slope is less than a fourth constant; andwherein the control is decreased upon deactivation of the reload subroutine. 25. The method of claim 16, further comprising the steps of: running a reload subroutine that repeatedly increases the variable degree of opening of the control;wherein the reload subroutine is activated when the first refrigerant temperature is greater than the first refrigerant temperature target, when the first slope is greater than a second target slope setting, when the first slope is less than a second target slope setting, and when the first refrigerant temperature is less than a third constant;designating a first value for the third constant if the first valve is at a range of closed positions;designating a second value for the third constant if the first valve is at a range of intermediate positions; anddesignating a third value for the third constant if the first valve is at a range of open positions. 26. The method of claim 25, wherein the third constant is equal to approximately negative 1° C. 27. The method according to claim 16, wherein the evaporator is a storage evaporator configured to control a temperature within the ice chamber; andwherein the evaporator is located downstream from an ice maker evaporator that is configured to furnish the cooling effect sufficient to freeze water.
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