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MDI Emissions Reporting Guidelines for the ... - Polyurethanes

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<strong>MDI</strong> <strong>Emissions</strong> <strong>Reporting</strong> <strong>Guidelines</strong> <strong>for</strong> <strong>the</strong> <strong>Polyurethanes</strong> Industry<br />

The total emissions from equipment leaks will be equal to <strong>the</strong> emissions contributed from each gas<br />

valves, light liquid valves, light liquid pump seals, and connectors.<br />

For gas valves:<br />

For liquid valves:<br />

K gas = 1.87 x 10 -6 *(C mdi ) 0.873<br />

K liq = 6.41 x 10 -6 *(C mdi ) 0.787<br />

For light liquid pump seals, compressor seals, pressure relief valves, agitator seals and heavy liquid<br />

pump seals:<br />

For connectors:<br />

Where:<br />

K pump = 1.90 x 10 -5 *(C mdi ) 0.824<br />

K con = 3.05 x 10 -6 *(C mdi ) 0.885<br />

K gas = <strong>the</strong> emission factor <strong>for</strong> gas valves in kg/year-item<br />

K liq = <strong>the</strong> emission factor <strong>for</strong> liquid valves in kg/year-item<br />

K pump = <strong>the</strong> emission factor <strong>for</strong> liquid pump seals in kg/year-item<br />

K con = <strong>the</strong> emission factor <strong>for</strong> connectors in kg/year-item<br />

For gas valves <strong>the</strong> emissions can <strong>the</strong>n be estimated from <strong>the</strong> following expression:<br />

L gas = K gas * n gas * K mdi * t pr * 2.205 lb/kg<br />

Lgas = <strong>the</strong> annual losses from gas valves in lb/yr<br />

ngas = <strong>the</strong> number of gas valves<br />

Kmdi = <strong>the</strong> adjustment factor to <strong>the</strong> vapor pressure that is a function of<br />

<strong>MDI</strong> concentration in <strong>the</strong> feedstock and <strong>the</strong> temperature<br />

tpr = <strong>the</strong> total time in hours/year that <strong>the</strong> process is operating<br />

For liquid valves <strong>the</strong> emissions can <strong>the</strong>n be estimated from <strong>the</strong> following expression:<br />

L liq = K liq * n liq * K mdi * t pr * 2.205 lb/kg<br />

Lliq = <strong>the</strong> annual losses from liquid valves in lb/yr<br />

nliq = <strong>the</strong> number of liquid valves<br />

Kmdi = <strong>the</strong> adjustment factor to <strong>the</strong> vapor pressure that is a function of<br />

<strong>MDI</strong> concentration in <strong>the</strong> feedstock and <strong>the</strong> temperature<br />

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