System for estimating thermal stress of pressure parts

A system for measuring thermal stress of a pressure-tight tube having a metal portion and having a fluid therein according to a calculation cycle, comprising:

• means for measuring temperature of at least the other surface of said tube;
• temperature distribution calculating means for calculating distribution of temperature at positions equidistantly arranged in a direction of thickness of said tube on the basis of measured values including at least the measured value from said temperature measuring means of the outer surface temperature of the metal portion of said tube;
• thermal stress calculating means for calculating thermal stress of the metal portion of said tube on the basis of said calculated distribution of temperature;
• internal pressure stress calculating means for providing an internal pressure stress value obtained on the basis of the fluid pressure detected by a pressure detector in said tube;
• and current stress calculating means for adding said thermal stress calculated value and said internal pressure stress calculated value together to obtain a current stress calculated value;
• a fluid temperature detector for providing measured values of fluid temperature in said tube;
• and
• calculation cycle setter means for presetting the calculation cycle on the basis of said measured values of fluid temperature whereby said calculation cycles are made short when fluctuations in the measured values of the fluid temperature are large, and further whereby said calculation cycles are made long when fluctuations in the measured values of the fluid temperature are small.

A system for controlling the load of a boiler by measuring thermal stress of a pressure-tight tube having a metal portion heated by said boiler and having a fluid therein, comprising:

• means for measuring temperature of at least the outer surface of said tube;
• temperature distribution calculating means for calculating distribution of temperature at positions equidistantly arranged in a direction of the thickness of said tube on the basis of measured values including at least the mesured value from the temperature measuring means of the outer surface temperature of the metal portion of said tube;
• thermal stress calculating means for calculating thermal stress of the metal portion of said tube on the basis of said calculated distribution of temperature;
• internal stress calculating means for calculating an internal pressure stress value on the basis of fluid pressure values provided by a pressure detector in said tube;
• and current stress calculating means for adding said thermal stress calculated value and said internal pressure stress calculated value together to obtain a current stress calculated value;
• stress limit preset value setting means for presetting a stress which is estimated to bring about an allowable life consumption of said tube per operation mode;
• stress limit presetting means for providing a stress limit preset value for said tube;
• and
• means for comparing said current stress calculated value to said stress limit preset value, load change rate presetting means for selecting and providing an optimal preset load change rate value from a plurality of preset value, load hold signal generating means for providing a load hold signal, and a controller for controlling the load of said boiler and for receiving said load hold signal and load change rate preset value;
• whereby, when the current stress calculated value exceeds the stress limit preset value, a load hold signal is generated and delivered to the controller, while when the current stress calculated value is lower than the stress limit preset value, an optimal load change rate value is selected and delivered to said controller from said load change rate presetter.

A system for controlling the load of a boiler by measuring thermal stress of a pressure-tight tube having a metal portion heated by said boiler and having a fluid therein, comprising:

• means for measuring temperature of at least the outer surface of said tube;
• temperature distribution calculating means for calculating distribution of temperature at positions equidistantly arranged in a direction of the thickness of said tube on the basis of measured values including at least the measured value from the temperature measuring means of the outer surface temperature of the metal portion of said tube;
• thermal stress calculating means for calculating thermal stress of the metal portion of said tube on the basis of said calculated distribution of temperature;
• internal stress calculating means for calculating an internal pressure stress value on the basis of the fluid pressure detected by a pressure detector in said tube;
• and
• current stress calculating means for adding said thermal stress calculated value and said internal pressure stress calculated value together to obtain a current stress calculated value;
• stress limit preset value setting means for presetting a stress which is estimated to bring about an allowable life consumption of said tube per operation mode;
• stress limit presetting means for providing a stress limit preset value for said tube;
• means for comparing said current stress calculated value to said stress limit preset value, load change rate presetting means for selecting and providing an optimal preset load change rate value from a plurality of preset valves, load hold signal generating means for providing a load hold signal, and a controller for controlling the load of said boiler and for receiving said load hold signal and load change rate preset value;
• whereby, when the current stress calculated valve exceeds the stress limit preset value, a load hold signal is generated and delivered to the controller, while when the current stress calculated value is lower than the stress limit preset value, an optimal load change rate value is delivered to said controller from said load change rate presetter;
• and
• a calculation cycle setter for presetting the calculation cycle on the basis of said measured values of fluid temperature, whereby said calculation cycles are made short when fluctuations in the measured values of the fluid temperature are large, and further whereby said calculation cycles are made long when fluctuations in the measured values of the fluid tempeature are small.