MDI Emissions Reporting Guidelines for the ... - Polyurethanes
MDI Emissions Reporting Guidelines for the ... - Polyurethanes
MDI Emissions Reporting Guidelines for the ... - Polyurethanes
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14. Belts and Tire Cord<br />
<strong>MDI</strong> <strong>Emissions</strong> <strong>Reporting</strong> <strong>Guidelines</strong> <strong>for</strong> <strong>the</strong> <strong>Polyurethanes</strong> Industry<br />
A <strong>MDI</strong>/P<strong>MDI</strong> mixture is used in belt manufacturing as a hardener. In <strong>the</strong> manufacture of<br />
belts, part of <strong>the</strong> process is to run syn<strong>the</strong>tic cords through a vat solution containing a<br />
<strong>MDI</strong>/P<strong>MDI</strong> and toluene mixture and <strong>the</strong>n passed it through an oven to activate <strong>the</strong> bonding<br />
process between <strong>the</strong> syn<strong>the</strong>tic cord and isocyanate and dry <strong>the</strong> cord coating. The off-gases<br />
from <strong>the</strong> oven are passed through an incinerator or combustion device <strong>for</strong> destruction.<br />
Depending upon <strong>the</strong> process, <strong>the</strong> syn<strong>the</strong>tic cord <strong>the</strong>n goes through a number of various<br />
mixture dips and oven treatments. Once <strong>the</strong> cords have been treated, <strong>the</strong>y are wound on<br />
spools <strong>for</strong> use in <strong>the</strong> belt building process.<br />
The controlling parameters that influence <strong>the</strong> emission rate are <strong>the</strong> temperature, flow rate,<br />
concentration of <strong>the</strong> exit gas stream, reaction rate, and <strong>the</strong> unreacted fraction of <strong>MDI</strong>. The<br />
worst-case scenario is that <strong>the</strong> exit gas stream is saturated with all <strong>the</strong> <strong>MDI</strong> that is available.<br />
The <strong>MDI</strong> emissions can be calculated using <strong>the</strong> following <strong>for</strong>mula:<br />
L = (V air /359) * (273.15/T sp ) * 60 * (C mdi /1000000) * M W * k <strong>MDI</strong> * C f * R <strong>MDI</strong><br />
Where:<br />
L = <strong>the</strong> emissions in lb/hr<br />
Vair = <strong>the</strong> exhaust airflow rate in ft3 /min<br />
Tsp = <strong>the</strong> exhaust temperature in K<br />
Cmdi = <strong>the</strong> <strong>MDI</strong> concentration, in ppmv, in <strong>the</strong> exhaust air<br />
MW = <strong>the</strong> molecular weight of <strong>MDI</strong> (250.26)<br />
K<strong>MDI</strong> = <strong>the</strong> adjustment factor to <strong>the</strong> vapor pressure that is a function of <strong>MDI</strong><br />
concentration in <strong>the</strong> feedstock and <strong>the</strong> temperature<br />
Cf = per cent <strong>MDI</strong>/P<strong>MDI</strong> in solution<br />
359 = <strong>the</strong> molar volume of an ideal gas in ft3 /lb-mole @ 0 o<br />
C and 1-atmosphere<br />
Cmdi = (VP<strong>MDI</strong> /760) x 10 6<br />
VP <strong>MDI</strong> = <strong>MDI</strong> vapor pressure at exhaust temperature<br />
R <strong>MDI</strong> = Unreacted fraction of <strong>MDI</strong><br />
Where:<br />
R <strong>MDI</strong> = e^(-k * t R )<br />
Where:<br />
R <strong>MDI</strong> = <strong>the</strong> unreacted fraction of <strong>MDI</strong><br />
k = <strong>the</strong> first order reaction rate constant in min -1<br />
t R = <strong>the</strong> reaction time in minute<br />
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