p. 1



# OAR Box 

# 1384 Prepped by Charmelle Mathews



## Document

Number: 

# l^0fj)ll-E-16 O Docket Number: 

# A-94-5 2

Printed 7/2/2008 8:42:10 AM

Sheet 200 of 264P. 2

00/24/100 0 00:3 2 001230454 0 oxroR D CM r IN C PAG C 0 2
0818-9 8 16:1 6 Olfl l 0041023. 1 PE S RT P N C ©002-00 5



## A 9 4 52 ,

From : Date : Contact ; Company : 

### Contac tRepor t Rober tJemison , Pacifi c Environmenta l Services , Inc . (PES ) Jun e 18,199 8 Mr . Thoma s E . Ebe i Oxfor d CMP. Inc . Telephon e Number : (601 ) 234-840 5 Ta x Number : (601)236-454 0 Contac tSummary : Mr . Thoma s Ebe r wa s contacte d o n behal f o f the U.S . HH

A t o updat e informatio n provide d i n the 1993 EP

A Reinforce

d Plastic Composites Screening Surve y submitted b y Oxford CMP , Inc . fo r their facilit

y located in Oxford, Mississippi . I n response t

o m y question s Mr

. Ebe r indicate d di e following : Th e facilit y use s polymer casting an

d atomize d spra y lay-u p (ge l coat

s only ) t o produc

e hat h tubs , bathroo

m vanit y tops , whirlpools , panels , showe r bases , columns , an d miscellaneou s tri

m pieces . Th e facilit

y use s atomired spra

y lay-u p (vi a a n HVL P spra y gun ) t o appl y a clea r ge l coa

t in the fabricatio

n o f th e product

s liste d above . Th

e facilit y doe s notus e pigmente d productio n ge l coat s i n di e fabricatio

n o f an y product . Th e clea r ge l coa tuse d b y th

e facilit y contain s SO.0 % HAP b y weigh t(SO.0 % styren

e an d 0.0 % methy

l methacrylate) . N o additiona l HA P i s adde

d l o thi s clear ge l coa tdurin g o r prio r to th e fabricatio

n proces s wit

h th e exceptio n o f

smal l amount

s o f HA P tha t ma y (o r ma y not ) b e presen

tin initiators , promoter

s and/o r catalyst s adde d t o th e clea r ge tcoat . The facility use s a castin g machin e t o conduc

tthe mixin g an

d polyme r castin g operation s necessar y t o produc

e the product

s liste d above . Th

e resin , filler , an

d catalys tar

e mixe d i n a mixin g lub e tha i i s located insid e di e castin g machine . The casting machin e i s completel y close d durin g th e mixin g operation . After th e mixin g proces s i s completed th e resultin g mixture i s ejecte d fro m the castin g machin e int

o a n empt y open mol d (o r molds) . Hi e polyeste r resi n use d b y th e facilit y fo r its polymer castin g operation s contain s 30.43 % HAP b y weigh tas supplie d (30.43 % styrene an d 0.0 % methy

l methacrylate) an

d doc s no tcontai n a vapo r suppressant

. N o additiona

l HA P i s adde d t o the polyeste r resi n during or prio r t o th e polyme r castin g proces s wit h th e exceptio n o f

smal l amount s o f HA P tha tma y (o r ma

y not ) b e presen ti n initiators , promoter

s And/o r catalyst s adde d t o the resin . Th e facilit

y ha s reduce d th e gel tim e o f th e polyeste r resin from approximatel y 30-4 0 minutes t o approximately 12-1 4 minute s i n uide i t o reduce the amoun to f HAP emitted durin

g th e curin

g process . INFORMATION I S ACCURATE 

# s^Us^j T £J&<^P. 3

00/24/100 0 00:3 2 001230454 0 OXTOR D CM P IN C PAG E 0 3 *«,,«,<, « ».,» , o'moouoca * rt s irr r N C fcoos-oos

Mr . Thomas E . Ebe

r - Oxfor d CMP . Inc . Jun e 18,199 8 Pag e Tw o
Th e facility use s th

e proces s o f

han d lay-u p (bucke t< k brush ) t o appl y a polyeste r resi n i n th e manufactur

e o f molds . Th e mold s ar

c use d onl y b y th e facility . Th e polyeste r resi n use d fo r mold manufacturin

g contains 50.0 % HA

P b y weight(50.0 % styien e an d 0.0 % methy l meihacrylate) . N o additiona

l HA P i s adde d t o the polyester resi

n durin g o r prio r t o th e mol d manufacturing prowes s wit h th e exceptio n o f

smal l amount s o f HA P tha tma y (or ma y not ) b e presen

ti n initiators , promoter

s and/or catalyst s adde

d t o th e resin . Th e facilit

y use9 atomize d 9pra

y lay-u p (vi a a n HVL P spra y gun ) t o appl y a pigmente d toolin g ge l coa

ti n th e manufactur

e o f th e molds discusse d above . Th e toolin g ge l coa tuse d b y th e facility contain s "W.0

% t e 41.0 % HA

P b y weight(39.0 % t

o 41.0 % styren e an

d 0.0 % methy l methacrylate) . N o additiona l HA P i s adde d t o thi s toolin g gel coatdurin g or prio r t

o th e fabricatio n pioces s wit

h th e exceptio n o f

smal l amount s o f HAP tha tma y (o r ma y not ) b e presen ti n initiators , promoter s and/o r catalysts adde

d t o th e toolin g gel coat . INFORMATIO N I S ACCURAT E >_^/_9^^J £ fjPCj



# 1*'.J06/24/199 8 06:3 2 601236454 0 OXFOR D CM P IN C PAG E 0 1 

# OXFOR D V/.CMP , INC

- mmaw PHON E 601-234-840 5 • FA X 601-236-454 0
» a INDUSTRIA L PAR KDRIV E • OXFORD

. M S 38S55 

# FA X COVE R LETTER Phon e No. : (601 ) 234-S40 5 Fa x No. : (601 ) 236-154

0

Date : < £ " ^ ~ ^C ? Time : £>< 36 #7* CCST 

## TO.- : fio*6>fi-r

777. rTeifiA-eiAj' Company : ]r

CIS FROM : v J M c /jjp 7 /
MESSAGE : A/<?7l*r/s 7AT_T &AJ



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