Control board systems and methods for diagnosis of HVAC components
US-12066210-B2 · Aug 20, 2024 · US
US10209141B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10209141-B2 |
| Application number | US-201314894807-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2013 |
| Priority date | May 31, 2013 |
| Publication date | Feb 19, 2019 |
| Grant date | Feb 19, 2019 |
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A method for determining the degree of heat treatment of a liquid product in a liquid product processing system involves measuring at least a first value representing the temperature of the liquid product within a first time period; measuring at least a second value representing the flow of the liquid product within the first time period; and calculating at least a first heat treatment index value based on the first and second values, wherein the heat treatment index value is associated with a current degree of heat treatment of the liquid product.
Opening claim text (preview).
The invention claimed is: 1. A method for determining a heat treatment index value for a liquid product in a liquid product processing system, the method comprising: measuring at least a first value representing the temperature of the liquid product within a first time period; measuring at least a second value representing the flow of the liquid product within the first time period; calculating at least a first heat treatment index value for the liquid product based on said first and second values and a predetermined pH value of the liquid product, wherein said heat treatment index value is associated with a current degree of heat treatment of the liquid product; and presenting the calculated first heat treatment index value to an operator of the liquid product processing system for monitoring. 2. The method of claim 1 , further comprising comparing the at least one heat treatment index value with a predetermined heat treatment reference value, and based on said comparison calculating a value representing a momentary degree of heat treatment of the liquid product for the first time period in view of the heat treatment reference value. 3. The method of claim 1 , wherein the measuring of the at least first value, the measuring of the at least second value, and the calculating of the at least first heat treatment index value are performed continuously or at regular predetermined intervals, thereby resulting in a set of first values, a set of second values, and a set of first heat treatment index values. 4. The method of claim 1 , further comprising calculating an accumulated degree of heat treatment of the liquid product by integration or summation of at least the first calculated heat treatment index value and a second calculated heat treatment index value over time. 5. The method according to claim 1 , wherein at least one of the at least one first value and at least one of the at least one second value are measured in a heat treatment unit by at least one sensor unit. 6. The method according to claim 5 , wherein a first sensor unit is positioned in at least a first section of the heat treatment unit and a second sensor unit is positioned in at least a second section of the heat treatment unit that is different from the first section of the heat treatment unit, the first sensor unit and the second sensor unit measuring at least one of a temperature and a flow rate of the liquid product. 7. The method according to claim 4 , wherein said accumulated degree of heat treatment is calculated by integrating or summation of a first heat treatment index value measured at said first section, and a second heat treatment index value measured at said second section. 8. The method according to claim 7 , wherein said first heat treatment index value is calculated at a first time, and said second heat treatment index value is calculated at a second time, and wherein a time difference between said first time and said second time corresponds to the time for a predetermined amount of liquid product to flow from said first section to said second section. 9. The method according to claim 8 , further comprising performing a second measurement of a first value and second value during a second time period being determined by the measured second value for the first time period and a downstream position at which the second measurement is conducted. 10. The method according to claim 1 , further comprising sending an alarm signal whenever at least one calculated or accumulated heat treatment index value is determined as not being food safe. 11. The method according to claim 1 , wherein the at least one first heat treatment index value is further calculated based on a predetermined parameter representing an interior contact surface of a heat treatment unit, through which the liquid products is flowing, per unit volume of liquid product. 12. The method according to claim 1 , wherein the at least one first heat treatment index value is calculated based on the formula: PIV ( t ) = t · 10 · ( T - T ref ) z , where t is the time in minutes, T is the current temperature of the liquid product, T ref is the required maximum temperature, and z is a liquid product constant. 13. The method according to claim 12 , further comprising calculating an accumulated degree of heat treatment index value as: PIV Acc. =Σ t=1 n PIV ( t ). 14. The method according to claim 1 , further comprising measuring a flow profile of the liquid product in a heat treatment unit of the liquid product processing system, wherein the at least one first heat treatment index value is further calculated based on the flow profile of the liquid product in the heat treatment unit of the processing system, through which the liquid products is flowing. 15. The method according to claim 5 , wherein the heat treatment unit is a heat treatment device that is one of a heater or heat exchanger, or a holding cell. 16. The method according to claim 1 , further comprising measuring a further second value representing the flow of the liquid product within the first time period and changing a required heat treatment temperature upon detection of a change of flow between at least the two second values. 17. A system for controlling the degree of heat treatment of a liquid product in a liquid product processing system, comprising: a first sensor unit for measuring at least a first value representing the temperature of the liquid product within a first time period; a second sensor unit for measuring at least a second value representing the flow of the liquid product within the first time period; and control unit being configured to calculate at least a first heat treatment index value for the liquid product based on said first and second values and on a predetermined pH value of the liquid product, wherein said heat treatment index value is associated with a degree of heat treatment of the liquid product, the control unit controlling operating parameters of the liquid product processing system based upon at least the first heat treatment index value. 18. The system according to claim 17 , comprising the first sensor unit and the second sensor unit defining a first sensor pair positioned in at least a first section of a heat treatment unit of the processing unit through which the liquid products is flowing, and further comprising another first sensor unit and another second sensor unit defining a second sensor pair positioned in at least a second section of the heat treatment unit. 19. The system according to claim 15 , wherein the heat treatment unit is a heat treatment device that is one of a heater or heat exchanger, or a holding cell. 20. A liquid food product manufactured using th
for measuring temperature of moving fluids or granular materials capable of flow · CPC title
between an inlet and an outlet point, combined with measurement of rate of flow of the medium {if such, by integration during a certain time-interval} · CPC title
Physics · mapped topic
of moving liquids · CPC title
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