Document wDbd9oD7Y9Ob4agaY4vZb6o9J

innr~\ I ?n rn MONOCKERfl INC. POST OFFICE SOX 486 ATON ffOUOt TELCAHOHC *04 14|.M1 GEISMAR.; IOUISIANA -70734 OUT^HTOWM telephone j.99* i 1--' October 14, 1971 RLS Mr. 6. A. Anderson UNIROYAL Chemical Division of UNIROYAL, Inc. Naugatuck, Connecticut 06770 Mr. J. V. Lynn Borden, Inc. 50 West Broad Street Columbus, Ohio 43215 Gentlemen: Subject: Vinyl Chloride Monomer Specifications and Typical Analyses For your information I would like to give you an updated look at Monochem monomer quality with a few comments. Typical Production______ Contaminant Specification New Catalyst Old Catalyst Acetaldehyde 5 ppm max. Acidity as HC1 10 ppm max. Appearance C&C Iron 0.5 ppm max. Sulfur 3 ppm max. Water 100 ppm Acetylene 2 ppm max. Isobutane No spec. N-butane No spec. Propadiene 5 ppm max. Butene-1 No spec. Methyl acetylene 2 ppm max. Butadiene 6 ppm max. Methyl chloride No spec. Vinyl acetylene 0.3 ppm max, 2 chloropropene-1 No spec. Methane No spec. Ethane or ethylene No spec. Propane No spec. Propylene No spec. Butene-2(trans.) No spec. Butene-2(cis.) No spec. Ethyl chloride No spec. 0.1 0.1 CSC 0.03 1.0 -24-30 ppm- ND -1-1 1/2 ppm-5-10 ppm-- ND 2 ppm 1 ppm 1 ppm 0.5 ppm ND ND ND ND ND ND ND ND ND 0.1 0.1 CSC 0.03 1.0 ND ND 10 ppm 2 ppm 4 ppm 0.5 ppm ND ND ND ND ND ND ND ND ND c 30 00 C<0O0) We have on occasion reported the presence of vinyl acetylene; we now know that this component is not vinyl-acetylene but is 2-chloropropene-l. A slight breakthrough in analytical technique has brought this to o attention. pois Dr A*SAFETy AND iiNT protection l I *\ T V Mr. 6. A. Anderson Mr. J. V. Lynn October 14, 1971 You will notice that catalyst age; i.e., higher catalyst temperature* causes a slight downgrading of the monomer in that butene-1, methyl acetylene and butadiene all tend to be in higher concentrations and therefore more difficult to remove. .Butane and iso-butane indicate the degree to which we are pushing the acetylene plant. We now have recharged the reactors so the monomer we are now producing will be as shown under the new catalyst column with a slight downgrading toward the old catalyst column over a two-year period. cc: Mr. J. S. Bellecci jadfc R. Little Vice President in Charge of Operations URL 18397 fc \