Humidity Measurement Benefits in Power Applications

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Presentation transcript:

Humidity Measurement Benefits in Power Applications Electric Power Conference April 21, 2016 Jeff Bossong, H2O jeff.bossong@h2oop.com 847-991-7488

Objective of Presentation H2O Technology Power Plant App

H2O Technology Absolute Humidity Sensor Advantages Direct measurement of the water molecule Dipole moment measuring effect In-situ measurement Advantages High temperature operation – 1000 F High particulate operation Minimal maintenance Corrosive and condensing environments are not an issue Accurate Robust (sensor life is 10 years minimum)

Installation Requirements Probe sizes – 490 mm or 1,470 mm lengths Flange - 4 inch, 150 lb ANSI Power – 110V, 5 Amps Output Signal – 4..20 mA isolated Measurement unit – g/m3 corrected to 0C at process pressure Other Units – Equations are provided (i.e., dewpoint, RH, humidity ratio)

Picture / Drawing

Installation

Power Plant Applications Coal / Biomass Fired Boilers Tube leak detection Soot blower feedback Heat rate calculations Air heater in-leakage Dry scrubber control Environmental reporting Wet scrubber stack protection Optimization Software Input Pulverizer control Combined Cycle Tube leak detection Dew point measurement Feed water Temperature control Environmental reporting Power Augmentation Optimization Software Input

Combined Cycle Tube Leak Detection – HRSG Outlet Our detection limit is 0.1 g/m3 at 0C Volumetric flow rate: 1,300,000 m3/hr Detection limit = leak / volumetric flow rate Leak = .1*1,300,000 Leak = 130,000 g/hr Leak = 4.78 lbs/min or 0.57 gallons per minute Process noise includes ambient humidity Could be used in conjunction with acoustic systems – lower detection limit-acoustic fines location

Combined Cycle Dewpoint Measurement – HRSG Outlet Water Dewpoint equation Pd = (1-(0.0001*(SQRT((0.1*T)+1)+4)))*461.51*(T+273.15)*F*0.00001 Dp = (234.175*LN(Pd/6.1078))/(17.08085-LN(Pd/6.1078)) T = Temperature in C F = Absolute humidity at process conditions Pd = Water vapor pressure Dp = Dewpoint temperature Water dew point temperature varies 111 to 120 F Corrosion prevention during outages

Water Dewpoint Temperature

H2SO4 Determination Verhoff & Banchero Formula Tds = 1000/(2.276 - 0.0294 ln(p H2O) - 0.0858 ln(p SO3) + 0.0062 ln(p H2O) ln( p SO3)) Partial pressures are expressed as mmHg Use humidity sensor as a direct input to equation Use worst case constant for SO3 concentrations Varies six degrees as a function of H2O concentration

Verhoff Chart – NG-CC

Sulfur Dewpoint Data - CC SO3 PPM H2O % Tds (Celsius) Tds (Farenheit) 0.1 9 95.02302265 203.0414408 10 96.2719508 205.2895114 12 98.49671327 209.2940839 0.5 108.4980274 227.2964494 109.68744 229.4373921 111.8008703 233.2415665 1 114.6077618 238.2939712 115.7679809 240.3823657 117.8288282 244.0918907

Verhoff Chart – Coal Plant

Sulfur Dewpoint Data - Coal SO3 PPM H2O % Tds (Celsius) Tds (Farenheit) 1 9 114.6077618 238.2939712 10 115.7679809 240.3823657 12 117.8288282 244.0918907 5 129.5780044 265.240408 130.6603171 267.1885707 132.5811611 270.6460899 136.3876155 277.4977079 137.4314954 279.3766918 139.2834203 282.7101565

Combined Cycle Environmental Reporting - Stack Provides real time, accurate moisture concentration EPA method 4 is not very accurate and data is a snapshot Could hurt or help depending on humidity number used for reporting Power Augmentation – Turbine Inlet Improved accuracy of dewpoint temperature Reduce factor of safety so inlet temperature can be lowered without condensation Optimization Software Input EtaPro, Neuco, Smart Burn, GE Optimization

Coal / Biomass Tube Leak Detection – Economizer Outlet Our detection limit is 0.1 g/m3 at 0C Volumetric flow rate: 372,000 m3/hr Detection limit = leak / volumetric flow rate Leak = .1*372,000 Leak = 37,200 g/hr Leak = 1.37 lbs/min or 0.17 gallons per minute Process noise includes ambient humidity, soot blows and fuel moisture More process noise but lower air flow

Coal / Biomass Economizer Outlet Soot blower feedback Safety to assure steam is firing Protect lances from bending and plant shutdown Heat rate calculations Fuel moisture variation Air heater efficiency Optimization Software Input

Coal Biomass Air Heater In-Leakage Rate – Economizer Outlet and Air Heater Outlet Water doesn’t stratify like oxygen: more accurate, real time leakage rate Equation AHI * y + AHA * x = AHO * F , where F=x+y x = (AHI-AHO)*F/(AHI-AHA) AHI = H2O reading at air heater inlet AHA = ambient humidity in g/m3 (manual or real time) AHO = H2O reading at air heater outlet F = flow leaving air heater x = volumetric leakage rate y = flow entering air heater No flow measurement will still provide a relative difference

Coal Biomass Dry Scrubber Control – Scrubber Outlet, Baghouse Outlet or Stack Control to an approach to adiabatic saturation temperature Better SO2 removal at lower temperatures improves lime usage Protects baghouse from corrosion Moisture variables include sootblow, load change, fuel moisture, ambient air humidity and tube leaks Dewpoint can vary up to 10 degrees depending upon time of year and conditions

Coal / Biomass Environmental Reporting – Stack Improved accuracy of emissions Could hurt or help depending on humidity number used for reporting Wet Scrubber Stack Protection Control reheat or bi-pass after scrubber Water carry over can increase moisture concentration past scrubber outlet dewpoint

Coal / Biomass Pulverizer Control – Pulverizer Outlet Sensor is a real time input for mass and energy balance across the pulverizer Sensor will also identify upset conditions, i.e. air flow upsets Dryer Control – Dryer Outlet Same as above

Thank You – Questions?????