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Control of Volatile Organic Compounds Emissions from Manufacturing

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Mr. Jack R. Fanner., Chief<br />

July 19, 1982<br />

Paoe -2-<br />

polymer manufacturing process. The major components to condense are styrene<br />

and ethyl benzene. Their vapor pressures at 60°F and atmospheric pressure<br />

are 3.5mms and S.Omms respectively, and this low vapor pressure enables them<br />

to be readily condensed even at low concentrations in a vapor- stream. Condensation<br />

is believed to be an accepted mode <strong>of</strong> control in a majority <strong>of</strong> the<br />

- bulk polystyrene facilities in use in the United States. , .<br />

. . . . , . ,<br />

. .<br />

:. .<br />

. , . . . . . . . .<br />

. - Monomer Recovery<br />

. .<br />

.<br />

. . . . . .<br />

. , . . . , .<br />

. . . . .<br />

. .<br />

.<br />

. . .<br />

.:I<br />

,<br />

; To 'achieve kry'measure <strong>of</strong> pr<strong>of</strong> irabiliry in the'.polystyrene .industry, .it is, .: :.'. '.' :<br />

very important to.-maximize the' recovery <strong>of</strong> unused monomk. . Recovered monomer ' .<br />

. can normally be reused,, after purilfication,,<br />

- . ~. . . ...<br />

. . , . .<br />

.. ,<br />

, .<br />

and must be success full^ recycled. ......<br />

,<br />

, '.to achieve pr<strong>of</strong>itable results. ::,., . . . . . ...<br />

. . .<br />

....... ... ....<br />

. . . . . . . ,,. ...<br />

. . .. : . . . . . . . . . ..;....... '". :<br />

,<br />

. . . . . ....<br />

. . . . . . . . . . . . .... ,<br />

'<br />

condensing unused monoier <strong>from</strong> the vapor phase which is' i n the' , , , ,<br />

',lastphase"<strong>of</strong> the process is,. therefore,"an. absolute findncial necessity. :.. .: ,.:<br />

- . . . ......<br />

. . . . . . . . . . .. : ....<br />

. .......<br />

..'. :to,the 'qccessful;;operation.<strong>of</strong> _ ._<br />

a'polystyrene.process. .<br />

, . I :. . . ,<br />

.. . .<br />

. . . ., . ...... . .<br />

,<br />

... ' .. . . . . . . . . . . . . . . . .<br />

:. . . . . . . ...<br />

. . . . . . . . . . _ . . .. .- .<br />

I_<br />

. ...;.... - ........ .: ........-:.-... ..;:..'.:...... :rene faciliiies Zo be reduced to below the recommended<br />

RACT - (Reasonably .bailzble <strong>Control</strong> Technology) referred to in the CTG <strong>of</strong><br />

0.3 kgs per 1000 kgs or' producr.<br />

-__.._- ...... , . .<br />

The attached information was taken <strong>from</strong> reports which were ap~roved.by the State<br />

.emfronmental agency in Korceseer, Massachusetts, before the construction <strong>of</strong><br />

a new Polysar facility for p.olystyrene nanufacture. The ,technology used in. .<br />

this facility to achieve the emission control levels shown is purely based" :<br />

on the condensation t i ~ erechnol.ogy discussed in this letter, and.clearly :<br />

illustrates the ability <strong>of</strong> this technology to achieve the conirol.required.<br />

The data submitted is theoretical and will: be further substantiated. during<br />

the initial operation: <strong>of</strong> the new facility: - ,. .<br />

Based: on the information submitted wizh this letter concerning the emissions<br />

<strong>of</strong> the latest Polysar facility in Leominster, Mas..sachusetts, ,l,,believe.-"itis<br />

readily apparent %hat the trse <strong>of</strong> .an incinerator ,i,snot required' dr;e to the<br />

snail irolune .........- <strong>of</strong> emissions actually discharged.<br />

. . . .<br />

: ej-.35 Y<br />

-. .. ,<br />

a .<br />

, .

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