Gyratory crusher hydraulic pressure relief valve
US-10478823-B2 · Nov 19, 2019 · US
US9494319B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9494319-B2 |
| Application number | US-201313834780-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 15, 2013 |
| Priority date | Mar 15, 2013 |
| Publication date | Nov 15, 2016 |
| Grant date | Nov 15, 2016 |
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A system for detecting a combustion-related condition in a pulverizer includes a pulverizer configured to receive coal chunks via an inlet, to grind the coal chunks into coal powder and to output the coal powder via an outlet. The system includes sensors configured to detect heat input characteristics supplied to the pulverizer and heat output characteristics emitted from the pulverizer. The system also includes a controller configured to determine, based on signals from the sensors, whether a combustion-related condition exists in the pulverizer based on a heat balance function including the heat input characteristics and the heat output characteristics.
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What is claimed is: 1. A method for detecting a combustion-related condition in a pulverizer, the method comprising: measuring, with sensors, input heat characteristics of a pulverizer and output heat characteristics of the pulverizer; and detecting a combustion-related condition in the pulverizer by performing a heat balance operation including the input heat characteristics and the output heat characteristics; wherein the heat balance function is: ∑ i = 1 out n m . i h i + ∑ j = 1 in k m . j h j = ∑ Q . , wherein m j is mass flow of air into the pulverizer, m j is mass flow of air out from the pulverizer, h j is enthalpy input to the pulverizer h j is enthalpy output from the pulverizer and Q is a change in energy, and wherein the detecting the combustion-related condition includes determining that Q is greater than a predetermined threshold. 2. The method of claim 1 , wherein the detecting the combustion-related condition in the pulverizer includes; calculating a difference between a combination of the input heat characteristics and a combination of the output heat characteristics; and determining that the difference is greater than a predetermined threshold. 3. The method of claim 1 , further comprising: controlling the pulverizer to reduce a magnitude of the combustion-related condition based on detecting the combustion-related condition in the pulverizer. 4. The method of claim 1 , wherein the heat input characteristics include a temperature and a humidity level of drying and transport air at a drying and transport air inlet of the pulverizer configured to flow the drying and transport air upward from beneath a coal grinding bowl of the pulverizer. 5. The method of claim 1 , wherein the heat input characteristics include a temperature and humidity of air input to a coal chunk inlet and heat generated by grinding the coal chunks into coal powder, and the output heat characteristics include a temperature and humidity of air at an outlet of the coal powder, a heat radiation of the pulverizer and a heat convection of the pulverizer. 6. The method of claim 1 , further comprising: monitoring a humidity of air at a coal powder outlet of the pulverizer to determine whether a precursor condition to a flame in the pulverizer exists based on a humidity level above a predetermined threshold. 7. The method of claim 1 , further comprising generating an alarm upon the detection of the combustion-related condition. 8. The method of claim 1 , wherein the combustion-related condition is a flame or smoldering. 9. The method of claim 1 , further comprising: receiving coal chunks into the pulverizer via an inlet; grinding the coal chunks into coal powder; and outputting the coal powder via an outlet. 10. The method of claim 1 , further comprising: grinding the coal chunks in a grinding bowl into coal powder; and supplying drying and transport air around the edges of the grinding bowl through a drying and transport air inlet located beneath the grinding bowl; wherein the heat input characteristics measured by the sensors include a temperature and a humidity level of the drying and transport air at the drying and transport air inlet. 11. The method of claim 1 , wherein the measuring the heat characteristics of the pulverizer includes: measuring the temperature of a housing of the pulverizer to determine a convection heat of the housing. 12. The method of claim 1 , wherein the measuring the heat characteristics of the pulverizer includes: measuring the temperature of a housing of the pulverizer to determine a heat radiation of the housing. 13. The method of claim 1 , wherein the measuring the heat characteristics of the pulverizer includes measuring heat characteristics, humidity characteristics and mass characteristics of air and solids into and out from the pulverizer. 14. The method of claim 1 , further comprising controlling the rotation of a drive assemby of the pulverizer upon the detection of the combustion-related condition. 15. The method of claim 1 , further comprising halting air inflow via an air inlet upon the detection of the combustion-related condition. 16. The method of claim 1 , further comprising halting coal chunk input via a coal chunk inlet upon the detection of the combustion-related condition. 17. The method of claim 1 , further comprising halting coal powder output from a coal powder outlet upon the detection of the combustion-related condition.
Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs {(high-speed drum mills B02C19/11)} · CPC title
Safety devices (in general F16P {; for rotary mills B02C13/31}) · CPC title
Mills with pressed pendularly-mounted rollers, e.g. spring pressed · CPC title
Control arrangements specially adapted for crushing or disintegrating · CPC title
Pulverizing · CPC title
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