Document MJ1J7MkRpO15rpQ8NDnVqOB3z
f FROM:R&D POLYMERS
IU:Ulb IH 1
To: PVC Overview Participants
I'lH^
J. J. X*+!-ir<
+-KJ ( -1
r . \fLSd.
:fe+h
fe
4
IntoroMlM
Communication
From:
Data:
J. L Irvine
Match 19, 1992
Subfact:
h
Agenda for the March 24 Training In Aberdeen
*
Attached is the Agenda for the PVC overview training next week in Aberdeen. We have you scheduled for this session. If you are supposed to be In the indepth training the tatter part of the week, lei me or Harold Coleman know and we will get you the correct agenda.
The times are approximate, except for the starting time. Class will be held in the training room of the plant Lunch wilt be provided. Dress casually and comfortably, if you want to go on the plant lour bring your safety gkmmy jf you have them. If you don't, they will be provided.
Be prepared in the
us what you expect from the class. We
can make small changes on the flyio make sure the class is a benefit to
everyone. At the end we will see if we were able to meet everyone's expressed need for the class.
We look forward to seeing you there.
John L Irvine
44
H n
VAB.0001191978
FRLTFK&D M-K-YntKta
I U* VXD ll-t
X
I II II N.
r
I*
RESIN/COMPOUND OVERVIEW AGENDA
I
8:00 8:15 9:15 9:30 11.00 11:30 12:30 2:00 2:30 4:00
Introduction
n
Resin Overview
Break
Resin Overview
//
Plant Tour
Lunch
Flexible Compound
i
Break
Rigid Com\\ pound *
Summary, Questions, Comments
Harold Coleman Harold Coleman
-
Harold Coleman
John Irvine
Randell Jackson HOC, JLI, RDJ
VAB.0001191979
*
rrsLji i * rs>cxu f ljl- f i k_is.cj
iu* viJin
To: PVC In-Depth Participants
in* n.
InttroNte#
CommunkoHon
From: Date:
J. L. Irvine March 19, 1992
Subject:
Agenda for the March 25-27 Training In Aberdeen
Attached b the Agenda for the PVC In-depth training next week in Aberdeen. We have you scheduled for this session. If you are not supposed to be In the in-depth training, let me or Harold Coleman know. Also let us know if we have you on the wrong day or days. Come to the sessions you are supposed to attend, not necessarily the ones where we have you listed.
The times are approximate, except for the starting time. Class will be held the training room of the plant. Lunch will be provided. Dress casually and comfortably. If you want to go on the plant tour bring your safety glasses if you have them. If you don't, they wit! be provided.
Be prepared in the introduction to telt us what you expect from the class. We can make small changes on die fly to make sure the class is a benefit to everyone. At the end we will see If we were able to meet everyone's expressed need for the class.
There will be a group dinner on Wednesday night, location still to be decided. If you are not in Wednesdays class and want to Join us, let me or Harold know so we can include you in the head count.
}
We look forward to seeing you there.
John L. Irvine
VAB.0001191980
RESIN/COMPOUND IN-DEPTH AGENDA
Wednesday, March 25
8:00
Introduction
8:15
Resin Production
9:30
Break
10:00
Resin Production Continued
11:30
Lunch
12:30
Resin Properties
2:00
Break
2:30 4:00
Resin Properties Continued
ra - ,
Resin Business^ai^Marketing
5:00
Break
6:00
Dinner "
Thursday, March 26
8:00
Resin and Compound Applications
8:45
Break
9:00 9:45
Resin and Compound Applications -1
Break
10:00
Resin Competitive Situation
11:00
Plant Tour
11:30
Lunch
12:30
Flexible Formulation Technology
1:30
Break
1:45
Flexible Formulation Technology
Harold Coleman Harold Coleman Harold Coleman
f John Irvine John Irvine Mike Clark
Harold Coleman John Irvine John Irvine
Randell Jackson Randell Jackson
VAB.0001191981
2:45
Break
3:00
Flexible Formulation Technology
Friday, March 27
8:00
Rigid Formulation Technology
9:45
Break
10:00
Compounding and Blending
11:30
Lunch
12:30
Compound Market and Business
1:30
Adlos
Randell Jackson Randell Jackson Randell Jackson Fred Williams
I l
VAB.0001191982
Tuesday
/ Sherry Truitt ^
t Jim White ^ > Greg Norman y Andy Wilson 7 Jimmy Autreyt/' Don Barclay v/
Mike Williams Debbie Botkin^ Steve Vrwv/ 7 Joe Beall 1/ Bob Seymour Sr <] Steve Hiifenan ib Linda Michels 1/
Wednesday
; * Ted Nickerson - Doug Skokna Amy Bagwell Erik Smith
jr Reed Mackay l Tim Arbeiter 1 Joe Ganc *
Rory Sneed Steve Vincent ? Duane Heaton Steve Kahara Mark Wolverton Charlie Muncy Carla Foshay Jill Wallace Ed Marshall Kenny Akins /* Mike McCollum // Roger drain - > ^ ^ Steve Goodman Carol Cooper Dan Miller Joseph Hegwood // Craig English // Mike Swierc /t Gary Wolf /7 Richard Williams / Doug Knittig /? Mike Clark
Thursday
Doug Skokna Amy Bagweil Erik Smith Reed Mackay Tim Arbeiter Joe Ganc Rory Sneed Steve Vincent ? Duane Heaton Steve Kahara Mark Wolverton Charlie Muncy Carla Foshay Jill Wallace Ed Marshall Kenny Akins Charles Woriow Mike McCollum Roger Crain Gary Wolf Debbie Lemmons Steve Goodman Carol Cooper Dan Miller Joseph Hegwood Craig English Mike Swierc Doug Knittig Mike Clark
Friday
Amy Bagwell Erik Smith Tim Arbeiter Joe Ganc Rory Sneed Duane Heaton Mark Wolverton Charlie Muncy Carta Foshay Jill Wallace Ed Marshall Charles Woriow Mike McCollum Roger Crain Gary Wolf Debbie Lemmons Steve Goodman Steve Hillman Dan Miller Joseph Hegwood Craig English Doug Skokna Mike Swierc Kenny Aldns Doug Knittig Mike Clark
A
VAB.0001191983
*
HIM
* ^PR
VAB.0001191984
PVC OVERVIEW
VAB.0001191985
PVC OVERVIEW
VAB.0001191986
PVC OVERVIEW
Introduction
- Definitions - PVC Market
Resin
- Markets - VCM Technology - Polymerization Chemistry - Polymerization Processes - Vista PVC Activities - Resin Properties
Compound
- Flexible - Markets - Formulation - Manufacturing - Testing - What's New
Rigid
- Markets - Formulation Manufacturing - Testing - What's New
Vista Polymers Research
Summary
A
VAB.0001191987
i
0
i
Definitions
1. Monomer - A low molecular weight molecule capable of being combined with itself or other similar molecules to produce a polymer.
- A macromolecule consisting of 5 or more identical combining units called monomers.
3. Polymerization
ci Cl Cl
- A chemical reaction, usually carried out with a catalyst, heat or light, and often under high pressure, in which a number of relatively simple molecules
combine to form a chain-like macromolecule.
VAB.0001191988
Definitions (cont.)
h
4. Vinvl
- Refers to ail PVC-containing substances (e.g. copolymers containing VCM or floor tiles containing as little as 15% PVC are called vinyl).
5. PVC
Polymer produced from vinyl chloride monomer.
6. Resin
-Generally used for non-rubberlike polymers. Refers to the initial form of PVC. Never really pure. PVC resin always contaminated to some extent with initiator, stabilizer, suspending agents, and kill agents, combining units called monomers.
blend' - Dry free flowing powders containing all the
appropriate additives (e.g. stabilizers, plasticizers, j
etc.).
I
-Both dryblends and pellets can be rigid or flexible compounds.
VAB.0001191989
*
VAB.0001191990
US COMMERCIAL THERMOPLASTICS PRODUCTION 1990
TOTAL PRODUCTION - 46.8 BILLION POUNDS
BILLION POUNDS
RESINS
<
O 22
VAB.0001191991
n V*
POLYVINYLCHLORIDE - END USE
MARKET PERCENT
b
Ethylene
LCCP
>
VAB.0001191993
PVC Manufacturing Plants
Oklahoma City
Resin (5385 only)
Aberdeen
Resin (All MW's) Flexible Pellets (incl. PlenexTM) Rigid Blend (dryblend) Plasticizer
Blane Polymers
Flexible Pellets
Premiere Polymers
Flexible Pellets Flexible Blend (RotoflexTM) Rigid Blend (dryblend) Rigid Pellets (VistelTM, SuprelTM)
Visalia
Flexible Pellets
PVC MAJOR MARKETS - 1990 Source: Modern Plastics, Jan. 1991
CALENDERING Building & Construction Transportation Packaging - Sheet Electrical - Tape Consumer/Institutional Furniture/Furnishings SUB-TOTAL
EXTRUSION Pipe & Conduit Siding & Accessories Window Profiles Transportation Packaging - Film & Sheet Electrical - Wire & Cable Consumer/Institutional SUB-TOTAL
INJECTION MOLDING Building & Construction Transportation Electrical/Electronics Consumer/Institutional Other SUB-TOTAL
BLOW MOLDING (BOTTLES)
COMPRESSION MOLDING (RECORDS)
DISPERSION MOLDING
DISPERSION COATING
LATEXES
EXPORT
GRAND TOTAL
MM LBS 348 90 115 13 287 200 1053
3610 860 401
20
365 410 307
5973
182 10
135 73 20
420
381 65
937
9297
VAB.0001191995
TOTAL SALES (MM LBS) 588 611 658
CO CO CM
CO
LO
CO
QC LU
Q
QC LU CO
K MM CD
LU cr
QC LU
< CL
<
O
CL
LU O X
CL o
0 O LU
VAB.0001191996
Vista
Industry
0) o
<5 '
I I I i I 1 I I I I------- 1------- 1-------
ooooooooooooo
(M^OOfiOStOlO^OOCMr-
VAB.0001191997
* *1
>-
0>
T_
CO (O U)
oo Is- Is- ^ <o
I
wo
mm
omo o m in
O 00 N
CM 1-1-
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cd m o o co oo oo oo in co
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00
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CM
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in
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in
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co
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in
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(O 00 N r- CM CO r- co co i
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oo
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o
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CO < X CO (3
CO
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LU
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a.
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lu
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CL
O
LU
<
CO
U1
Q
CL
O
LU CL
$
CL
UJ
i--
O h" CO U- CD Q0XQQ.O
TOTAL
7230 -
11345 (604)
Modern Plastics, Jan. 1991
* INCLUDES ALL PLANNED EXPANSIONS
*
VAB.0001191998
NAMEPLATE CAPACITY 1/1/92*
SUPPLIER
SHINTECH OXYCHEM FORMOSA BFGOODRICH BFG 1993 VISTA GEORGIA GULF BORDEN WESTLAKE CERTAINTEED VYGEN
SUSPENSION
2000 1900 1789 1600 1100 840 810 795 500 265 125
DISPERSION
200
96 150 150
48 55
VAB.0001191999
VAB.0001192000
MORE
1. SOLUBLE IN ETHYL ALCOHOL, DIETHYL ETHER, BUT NOT WATER
2. VOLUME DECREASES WHEN POLYMERIZED BY 35% SAFETY
h
1. NARCOTIC
2. CAN CAUSE LOSS OF CONSCIOUSNESS AT HIGH CONCENTRATION
3. SUSPECTED CARCINOGEN A. ANGIOSARCOMA B. AOL - BONE DISORDER
4. TERATOGEN - FETUS AFFECTS IN PREGNANT WOMEN
5. OSHA LIMITS
1
A. 1 PPM OVER 8 HOURS
B. 5 PPM IN 15 MINUTES
6. MONITORS (BADGES) RECOMMENDED
7. FRESH AIR MASKS REQUIRED
HANDLING AND STORAGE
1. ORDINARY STEEL CONTAINERS 2. ONLY MILDLY CORROSIVE 3. MUST BE KEPT ACIDIC AND OXYGEN-FREE
VAB.OOOl192001
V; vf'
V *#x
i< ^5i*fV.= -<j-. .>v 4X >
,p pT-
^
J-p
*
%'i
*->
a.?-'--
A* ''f^e VlSi v^' ,
0.5 ppm 1.0 ppm
5.0 ppm
VAB.0001192002
* 5%V - -$ :`y-
!*
3 Tt / . H.
v *
*
Ov>* f\t;
I
\
400 ppm 20 Lbs
Vinyl Chloride Per Million Lbs. PVC Produced
10 ppm
POLYMERIZATION
VAB.0001192004
POLYMERIZATION STEPS
1) Initiation 2) Propagation 3) Chain Transfer 4) Termination
MECHANISM OF POLYMERIZATION
Initiation O
O
Free radical formation
ii
ii
R-0-C-0-0-C"0-R
o
II
R-O-C-O1
Propagation
note head to tall addition
o
2R-0-C-0' O HH
STRUCTURE DF PVC
HUn Un Url
un un un H
H HH H
wwc-c-c-c7XAAc-c-c -1CA-A/wA \^>cI -CI -CI ^wv
H C1H Cl
I I II I
Cl Cl H Cl H H Cl
HEAD-TO-TAIL
(98%)
HEAD-TO HEAD TAIL-TO-TAIL
MECHANISM OF POLYMERIZATION 3. Chain Transfer
HH
a^^'^C-CHCI
H1 rCi1
4. Termination
Recombination
HH HH
I1
1I
H C1 C1H
iIII
AAA_^
^W\
II
ci ci
INHERENT dL/grams VISCOSITY
NUMBER AVERAGE MOLECULAR WEIGHT
(grams/molt)
E
VAB.0001192009
MECHANISM
4. Termination
Disproportionation
POLYMERIZATION
I
AAA
II
I
Cl
CH
^AB.0001192010
POLYMERIZATION PROCESSES
MASS (BULK) EMULSION SOLUTION SUSPENSION
VAB.0001192011
MASS (BULK) POLYMERIZATION
Manufacturers:
Pechiney St. Gobain BFG - Plaquemine, LA Occi - Burlington, NJ
(closing down)
Two-stage batch process
Polymerization starts in VCM phase, then precipitates.
1. Very uniform, porous particles. 2. High bulk density. 3. Free of suspending agent and water contaminants. Disadvantages: 1. Difficult to control temperature (mol wt). 2. More expensive than suspension. 3. Difficult to strip residual VCM.
Markets: Same as suspension except for molding.
VAB.0001192012
EMULSION POLYMERIZATION
Manufacturers:
Borden BFG Occi Formosa Georgia Gulf
Process:
1. Soaps used to form "micelles" in water.
2. Water-soluble initiator encounters VCM in micelles.
3. Diffusion from monomer droplets to micelles replaces polymerized VCM.
Advantages:
t. Very uniform, small, nonporous particles.
2. Processes easily (plastisols) without much heat.
Disadvantages:
1. High contamination level of soap.
2. Poor heat stability.
3. High cost - energy intensive drying.
Markets: Plastisols - used for coatings and molding.
VAB.0001192013
DISPERSION POLYMERIZATION
Manufacturers: Occi (others?) Similar to emulsion, except:
1. Monomer soluble initiators.
2. No micelles are formed; instead, high mechanical shear is used in a preliminary step to form droplets.
Advantages: 1. Same as emulsion.
Disadvantages:
1. Same as emulsion.
Markets:
Same as emulsion. The terms "emulsion resins" and "dispersion resins" are used interchangeably in the industry. Resins used in plastisols can be made by either emulsion or dispersion processes.
VAB.0001192014
SOLUTION POLYMERIZATION
Manufacturers: Union Carbide Process:
1. Mostly P VC/poly vinyl acetate copolymers. 2. Polymerized in a solvent (n-butane), then
precipitates. 3. Not much is known about UC's process. Advantages: 1. Similar physical properties as bulk. Disadvantages: 1. High cost. 2. Solvent recovery/environmental. 3. Limited market.
Markets; Can liners.
VAB.0001192015
SUSPENSION POLYMERIZATION
Manufacturers: Vista and many others Process:
1. Mostly homopolymer, but some PVC/polyvinyl acetate copolymers.
2. VCM droplets suspended in water. 3. Initiator is monomer soluble. Advantages: 1. Easily controlled temperature. 2. Easily filtered and dried. 3. Low cost. Disadvantages: 1. Small change in conditions alters properties. 2. Not as pure as mass or solution. Markets: Extrusion, molding, calendering...
Virtually unlimited.
VAB.0001192016
THE SUSPENSION PROCESS
THE ROLE OF WATER 1. ACT AS A CONTINUOUS PHASE AND ENABLE VCM TO BE
DISPERSED 2. ACT AS A HEAT TRANSFER MEDIUM 3. CARRIER FOR PROTECTIVE COLLOID (SUSPENDING AGENT)
THE ROLE OF SUSPENDING AGENT 1. CONTROLS PARTICLE-SIZE DISTRIBUTION 2. KEEPS VCM DROPLETS DISPERSED 3. FACILITATES HEAT TRANSFER AND AGITATION
THE ROLE OF THE AGITATOR 1. PRODUCES DESIRED PARTICLE SIZE 2. MAINTAINS SUSPENSION DROPLETS AND PVC GRAIN 3. ENSURES GOOD HEAT TRANSFER
VAB.OOOl192017
THE ROLE OF THE INITIATORS
1. CONTROLS RATE OF POLYMERIZATION 2. CONTROLS RATE OF HEAT EVOLUTION 3. AFFECTS NUMBER OF GELS IN RESIN
CHAIN TRANSFER AGENTS
Function: Terminate Macroradical Chain and Initiate New Cha i n.
Effect:
Terminate Chains at Shorter Length Than Normal for a Given Temperature.
Purpose:
Allows Production of Low Molecular at Lower Temperature (and Pressures).
WE ight
PVC
VAB.OOOl192018
Ingredicuts: Munome r (s) Initiator Solubil ity Suspending Agent
Reactor Agitation
Market Rank (Lb. Basis) Mean Particle Diameter End Use
CHARACTERISTICS OF PVC POLYMERIZATION PROCESSES
Suspension PVC
Resin Polymerization Type
Emulsion
Mass or Bulk
PVC PVC
VCM VCM Protect 1ve Co 11 oid
High Shear
1st
150 pm
Rigid Flexible Extrusion Film Blown Calender Molding
VCM Water Soap
Low Shear
2nd
10 pm
Pastes Latex Dispersions Creams
VCM VCM None
High then Low
3rd
150 pm
Rigid Flexible Extrusion Film Blown Calender
Solution PVC
VCM/Vinyl Acetate VCM None
Low
Distant 4th Solution Beer Can Liners
VAB.OOOl192019
VISTA POLYMERIZATION PROCESS TECHNOLOGY
VCM
'VAB.0001192021
POL
iRIZATION
CHARGE POLYMERIZATION RECOVERY 8< STRIPPING
PUMP RINSE 8i CLEANING
EVACUATION
CYCLE
, HIGH PRESS 'water
POLY..FRIZAT ION SECTION PVC MANUFACTURE
VCM TO RECOVERY
RTKJCC UATRP AKjn
ULfc^NlNU bULU11UN
rCOOLING WATER ^SUPPLY
7
CITY WATER
CENTRATE
VAB.0001192022
*.
.f
CONDENSER
BAFFLES
VISTA REACTORS
JACKET
AGITATOR
STEAM STRIP
CENTRIFUGE DRYER SILO
0
VAB.0001192023
o5
o
u
Eh
< Eh
CO
D Q
o u
co A o H
CO
o
EH
fc
RESIN DRYING SECTION
CO o5
a s
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a
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w o 05 05
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M 05 Q
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05
aa
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05
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VAB.0001192024
VISTA RESIN GRADES (MOLECULAR WEIGHTS)
* With CTA
-i. > 'p* p
VAB.0001192025
pp-
fc
PVC RESIN APPLICATIONS
5225
Rigid Injection Molding
5265
Pipe Fittings
5305
Rigid Pipe Fittings Rigid Calendering Powder Slush Molding
5325
Powder Slush Molding
5385
Pipe Siding Profile extrusion
5395
General Flexible Applications Calendering . Molding
5415
Building Wire Communications Wire General Purpose Calendaring Flexible Automotive Molded Parts
5465
Automotive Wire Vinyl Car Tops Toys Electrical Tape
VAB.0001192026
*
Vista Chemical Company
1
Molecular Weight Measures of PVC Resin
From W. V. Tltow, PVC Technology, 4^* Edition
0.42 0.44 0.47 0.49 0.52 0.55 0.57 0.60 0.62 0.65 0.67 0.70 0.73 0.75 0.78 0.80 0.83 0.85 0.88 0.91 0.92 0.95 0.98 1.01 1.03 1.06 1.08 1.11 1.13 1.16 1.18 1.21 1.23 1.26 1.28 1.30 1.33 1.35 1.38
1.54 1.58 1.62 1.66 1.70 1.74 1.78 1.83 1.87 1.90 1.96 1.99 2.03 2.07 2.10 2.17 2.21 2.25 2.28 2.32 2.36 2.43 2.46 2.50 2.54 2.57 2.64 2.68 2.72 2.79 2.83 2.90 2.93 2.97 3.04 3.08
0.155 0.165 0.175 0.185 0.195 0.206 0.217 0.228 0.239 0.25 0.264 0.275 0.285 0.3 0.31 0.32 0.33 0.34 0.36 0.37 0.38 0.39 0^40 0.41 0.43 0.44 0.45 0.46 0.47 0.49 0.50 0.51 0.53
v- 0.54
0.56 0.57 0.58 0.6 0.61
45.3 46.2 47.1 48.4 49.3 50.1 51.3 52.4 53.6 54.7 56.1 57.2 58.2 59.5 60.5 61.7 62.9 64.1 64.9 66.1 67.1 68.2 69.2 70.2 71.5 72.4 73.3 74.3 74.9 75.8 76.6 77.5 78.3 79.1 79.9 80.7 81.5 82.2 83.0
275 310 350 380 415 450 495 525 560 600 640 680 720 760 800 840 885 930 975 1025 1070 1120 1175 1230 1300 1350 '1420 1490 1570 1650 1720 1810 1900 1980 2070 2170 2260 2360 2460
46,600
62,000 76,300 88,700
103,800 120,600 135,200
Vista is a registered trademark of Vista Chemical Company.
The above data are based on tests and experience which Vista Chemical Company believes reliable, and are supplied for informational purposes only Vista Chemical Company disclaims any liability for damage or injury which results from the use of the above data and nothing contained therein shall constitute a guarantee, warranty or representation (including freedom from patent liability) by Vista Chemical Company with respect to the data, the product described or its use for any specific purpose, even if that purpose is known to Vista Chemical Company For detailed information regarding these products, please refer to the respective Vista Chemical Company Material Safety Data Sheet.
i * i
VAB.0001192027
REACTOR SIZE
ABERDEEN
QKC
FOUR 18,000 GAL FOUR 22,000 GAL TWO 33,500 GAL
SIX 18,000 GAL
CAPACITY
ABERDEEN - 450 MM LBS/YR
5465
0 ( 0%)
5415 160 (35%)
5395
20 ( 4%)
5385
190 (42%)
5325 1-2 (< 1 %)
5305
50 (11 %)
5265
30 ( 7%)
5225 1-2 (<1%)
OKC - 350 MM LBS/YR
5385
350 (100%)
+ 1r
T3
VAB.0001192028
55 oo
o llOO
ooo 00
ooo
e* S
10
CO
<N
VAB.0001192029
POT YMF.RTZATTON RECIPES
4
VAB.0001192030
VISTA ADVANCES
LARGE REACTOR TECHNOLOGY STATISTICAL PROCESS CONTROL ADVANCED SUSPENDING AGENTS (RQIP)
- LICENSED FROM BASF FLUID BED DRYING ENHANCED COMPUTER CONTROL EXTENSION OF RESIN TECHNOLOGY - 5225 - 5325 - 5395 - 5416 (MORE POROUS 5415) CLEAN WALL TECHNOLOGY
- LICENSED FROM EVC NEXT: EXTERNAL STRIPPING
IMPROVED GELS/CONTAMINATION IMPROVED CONSISTENCY
A
VAB.0001192031
*1 * >
I i.w i. . .|i
W-' * . + 1 r I
*
A
1963 ACQUIRED CARLON FVC PIPE CO.
1964 ACQUIRED APEX TIRE AND RUBBER CO. (COMPOUND) AND THOMPSON CHEMICAL CO. (PVC RESIN) FROM FAIN FAMILY.
1964 EXPLOSION AND FIRE AT THE HEBRONVILLE MASS. PVC PLANT.
1964 ABERDEEN MISS. PLANT STARTED-UP AND THE ASSONET MASS. PLANT BUILT.
1967 R&D MOVED FROM PONCA CITY TO ASSONET MASS.
1968 VINATEX (ENGLAND) CAME INTO EXISTENCE.
1968 FTC MADE CONOCO DIVEST OF ITS ASSONET MASS. PLANT (SOLD TO OLIN INDUSTRIES) , COMPOUNDING FACILITIES IN RHODE ISLAND (SOLD BACK TO THE FAIN FAMILY <TECKNOR--APEX>) , AND BUY OUT STAUFFER PORTION OF THE VCM PLANT.
1968 CONOCO PLASTICS FORMED FROM CARLON PIPE AND PVC PLANT IN ABERDEEN AND HEADQUARTERED IN WILTON, CONN., INCLUDING R&D.
1970 LARGE REACTOR PLANT STARTED-UP IN OKLAHOMA CITY.
1972 SOLD CARLON TO INDIAN HEAD INDUSTRIES, SHUT DOWN THE WILTON FACILITIES, MOVED R & D TO PONCA CITY, AND FORMED CONOCO CHEMICALS.
1975 ALL SMALL REACTORS SHUT DOWN.
1976 DIVESTED OF OUR HOLDINGS IN VINATEX.
1978
to 1981
PVC RESIN, INCREASED.
DRY BLEND,
AND COMPOUND CAPACITIES
1984 VISTA POLYMERS INC. FORMED.
1986 VISTA POLYMERS COMBINED INTO VISTA CHEMICALS.
1986 PREMIERE POLYMERS ACQUIRED.
1987 BLANE POLYMERS ACQUIRED.
1988 VYCOM STARTED
1989 R & D MOVED TO AUSTIN/ABERDEEN.
VAB.0001192032
1k
I*--* I--'
EFFECT OF PROCESS VARIABLES ON RESIN PROPERTIES
A
Property A. Molecular Weight
(Inherent Viscosity) B. Particle Size Distribution
C. Bulk Density
D. Porosity (Brabender Dry Time, Cold Plasticizer
Absorption, Residual VCM)
E. Gels
F. Resin Color
G. Heat Stability
H. Moisture I. Electrical Properties
1*
Process Variable
1. Polymerization Temperature 2. Chain Transfer Agents 3. Chain Coupling Agents
1. Suspending Agent Concen
tration
2. Agitation
1. Static 2. Resin Particle Shape 3. Additives
1. Degree of Conversion of
VCM to PVC
2. Polymerization Temperature 3. Additives
1. Cleanliness of Reactor 2. Agitation 3. Additives
1. Heat History 2. Antioxidant
1. Heat History 2. Killing Agent 3. Antioxidant
1. Drying Efficiency
1. Type Initiator 2. Additives 3. Type Poly Water
vab.oooi 192033
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VAB.0001192034
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PVC PROPERTIES-- DRYER RELATED
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VAB.0001192035
VAB.0001192036
VAB.00011^2037
Market: Wire Cable
Applications: insulation. jacketing conduit power, communications, computer
Vista lbs:
108MM Ibs/yr (70% Vista Flexible)
Major Customers:
Times Fiber, AT&T, Northwire Tandy eneral Cable Allflex
FLEXIBLE COMPOUND
if i- .
i
*t% r r 'Ji-'
* i =. ..
^ .L-
s'
K^ulir . L-r. .h....
F
i. >.
VAB.0001192038
Application:
Window encapsulations
Vista lbs:
7MM Ibs/yr (5% of Vista Flexible)
Major Customers:
Donnelley, Deckerville
FLEXIBLE COMPOUND
* it-
t-
r, -
1 <4
l-i TMi-
i
- '-K
VAB.0001192039
I
I
Market: Weatherstripping
Vista
15MM Ibs/yr
(10% Vista Flexible)
Major Customers:
Central Plastics, Betterbuilt Vytron Macklanbura Duncan
FLEXIBLE COMPOUND
+
ii.
t +-
-I-
piw
,?(. ,
........ ... ,
VAB.0001192040
Other Uses/Markets
Flexible Hose and Duct Heating Pads Coated Fence Coated Yarn
4
*
T s A|
: id ..d. ^ -iff*' -li ***; :y.
d .* *r. *j
h.
I
VAB.00011 92041
Formulation
/ Flexible Compound * PVC Resin + Plasticizer + Other Ingreds.
/ Other ingredients added to improve performance properties processibility
Customize formulation to end-usey processing needs, and economics
FLEXIBLE COMPOUND
4
'I*-''
i'i
i'i I H` H . i .
I-
r-.r- I.IN- N
1 Hi'-N*-
PI Wlr-
I
I
VAB.0001192042
>!
i i i
Ingredients
!ny V'iiiOOt
PVC Resin
PR()
low cost low flammability
Plasticizer flexibility
Stabilizer
prevents heat degradation
Fillers
/
lowers cost
<, ^ /fa :
%
CC-'v
is-
}
low stability
flammability cost
inc. hardness r
dec. flex.
( 'V&-
FLEXIBLE COMPOUND
m
Ingredients
Lubricants
i
better processibilty
Flame Retardant^
flame resist, lower smoke
\Antifungal8/
reduce fungus
!\ Antimicrobials bacteria / /
Pigments
color
FLEXIBLE COMPOUND
A
cost toxicity can affect other properties
^ t *-
--.1 4<
- HM-s
. . *..y; =
^
-|J
' f Kl'm
L* * * l
AB.0001192044
Plasticizer
/ Gives PVC flexibility & rubbery feel
v
'/ Vista makes & purchases plasticizer / 108P & 610P made at Aberdeen from
alcohols shipped from LCCP Vista also sells & trades plasticizer
FLEXIBLE COMPOUND
J" 1
VAB.0001192046
i
3s>
Product: Wire Jacketing
liKjrpdient Resin Plasticizer Filler Stabilizer Flame Retardant Lubricant
Cost ($/lh 38 42 5 62
136 40
FLEXIBLE COMPOUND
i
if
i
ii
* .jw-h
I Vr . ( K
-H,
t -i-
I*
VAB.0001192047
1
k* .
inTiHir
fi-+r .--i -h. ,| ..
VAB.0001192048
i
_ Blend
MJiiL (MhLI )
< ;< A A
& <;u i
VAB.0001192049 3*>
p i
* - H'TI k- -
- -V, I
` L'WiWB fH
l
I 'll'
^AB.0001192050
LIQUID STABILIZER WEIGH
<nSCALE
L_
PLASTICIZER
(4)WEIGH TANK
ACTIVATOR
(I)
PVC RESIN POWDER FROM VINYL AREA
BULK PVC RESIN STORAGE BINS
(21
PLANT AIR
PLASTICIZER
00 PUMP(S41
EXHAUST
BUCKET CONVEYOR
INTERMEDIATE HOLD TANK (I) I HOPPER (I)
FILLER COLOR 1 MISC SMALL Additives HANO CHARGED TO BLENOER
A
BANBURY
MIX(IE) R
/ /
/
(I)
VINYL RIBBON
DICING SCREENING
AREA (2)
I------- 1 II *1 I
(iMMJDRIBBON
blenders
(2)
>
/
/
0-
WEIGH
SC(A2L) E
//
/
' COMPOUND CONVEYOR II) LINE I 'BUCKET
/
/
TWO ROLL CALANOERING
M(IIL)L
RIBBON COOLING
TRO(IUI GH
COOLING TANK
(I)
I'
XJ
PROOUCT PACKOUT STATIONS (2)
lb BAGS OR IOOO lb i
BLOWER
ABERDEEN LINE I SCHEMATIC
FIGURE 11
't -
-:i . !-!> Kjrjfr.
VAB.0001192051
k .
4l'l' fittrpivn%
*-< '
n >I
umn
, 'VAB.0001192052
Vista's Competition
< 'Ompany Vista
V
Capacity
(MM !L>s/yr)
260
% PVC. P!i 100,50
BF Goodrich
220 100,0
Tek nor-Apex
150 0,100
Cary
110 0,0
Gary
80 0,0
North American
75 0,0
!' *d1 > y Othbl iS
il
FLEXIBLE COMPOUND
VAB.0001192053
Testing
/ Why do w test? quality control product development certification
y Used to predict performance
/ Comparative tests /Test methodology - ASTM
FLEXIBLE COMPOUND
4
'T '-in
i
i
,i
I
>>VAB.0001192054
Tests
I'Mifuji ty Tested
Hardness (resistance to indentation)
Flexibility Strength
Resistance to Tearing
Electrical Properties
let, I
Durometer Hardness
Tensile (elongation) Tensile (strength) Tear strength Resistance
FLEXIBLE COMPOUND
ff
_ VAB.0001192055
VAB.0001192056
What's New?
/ Rotoflex 7 PlenexTM
FLEXIBLE COMPOUND
VAB.0001192057
What's New? Rotoflex
I '
m I
4
yDry* Flexible Blend
y Made with special ingredient that
absorbs excess plasticizer
/ Made at Premiere on dryblend unit
FLEXIBLE COMPOUND
I
>/ Used to make automotive interior "skins"
>/ Current customer: Toyota (Camry instrument
y Market potential: Ibs/yr in
y Powder
>4 'l
h ih
n |J
VAB.0001192059
4
What New? Plenex
Low smoke flame wire cable compound plenum applications / Plenum space:
area between false ceiling and floor in commercial buildings very strict smoke & flame requirements competition is flouropolymers
FLEXIBLE COMPOUND
t in *.
\^B.0001192060
h
VAB.0001192061
MARKETS FORMULATION MANUFACTURING TESTING WHATS NEW?
11
VAB.0001192062
4
VAB.0001192063
PVC PIPE
i
PRODUCTION PROCESS
-EXTRUSION
FINAL PRODUCTS
-POTABLE WATER (PW) -SEWER -DRAIN. WASTE AND VENT (DWV) -IRRIGATION -ELECTRICAL -COMMUNICATIONS CONDUIT -CORRUGATED DRAINAGE
VISTA PRODUCTS
-5385 -80273 -80174
IMPORTANT CONSIDERATIONS -COST -OUTPUT RATES
VAB.0001192064
PVC PIPE FITTINGS
PRODUCTION PROCESS
-INJECTION MOLDING
FINAL PRODUCTS
f
-COUPLING FITTINGS -'`TEE" FITTINGS -'ELBOW" FITTINGS
VISTA DRYBLENDS
-90171 -90172
IMPORTANT CONSIDERATIONS -HEAT STABILITY -MELT FLOW
iT
-t
... ........................................................
I"-
-1
.
|.. =, f-i.
- J;.j
-S 1
A' -ci-rfl'
*VAB.0001192065
ll.it-1- . . T
t'.L'i n -tai-i ! I L 1- -i . i . '1^ ..k . .
PVC
PRODUCTION PROCESS THIN SHEET THICK SHEET
FINAL PRODUCTS CALENDAR SHEET
EXTRUDED SHEET
VISTA DRYBLENDS
IMPORTANT CONSIDERATIONS
CALENDARING EXTRUSION
BLISTER PACKAGING CREDIT CARD STOCK FLOPPY DISKS
WALL COVERINGS SANITARY WARE ACID TANKS
RP 421 RP 442 RP 461
SURFACE APPEARANCE IMPACT STRENGTH
VAB.0001192066
VINYL
PRODUCTION PROCESS
-EXTRUSION
FINAL PRODUCTS
-HORIZONTAL SIDING -SIDING TRIM -CORNERS -SOFFIT
-INDUSTRIAL SIDING -MOBILE HOME SKIRTING
VISTA PRODUCT
-5385
IMPORTANT CONSIDERATIONS
-WEATHERABILITY -IMPACT STRENGTH -OUTPUT RATES -COST
PVC PROFILES
PRODUCTION PROCESS
-EXTRUSION
FINAL PRODUCTS INTERIOR PROFILES ('CUSTOM')
I
EXTERIOR PROFILES
-APPLIANCES -INTERIOR CONSTRUCTION -AUTOMOTIVE
-WINDOW FRAMES -DOORS -FURNITURE -MOBILE HOME SKIRTING -GUTTERS
VISTA PRODUCT
-RP 200T
IMPORTANT CONSIDERATIONS -SURFACE APPEARANCE -WEATHER ABILITY -IMPACT STRENGTH
VAB.0001192068
GOOD PROCESSING (EASE OF FABRICATION)
GOOD PROPERTIES IN FINISHED PART
OTHER (SECONDARY)
1 * 1`
VAB.0001192069
*:iH--sfll'J- : i L-*.'
rfi.
A
*
ALWAYS: RESIN STABILIZER LUBRICANT
USUALLY: PROCESSING AID IMPACT MODIFIER PIGMENT FILLER
1 * -i
' i"-1
h & . |J J ^l|
Fnil ..i
VAB.0001192070
*
Phr: Parts per Hundred Parts Resin
Reason:
Convenience for formulation development
Simple example:
5385
86
Stabilizer
2
Lubricant
2
Impact modifier 6
Filler
4
A
VAB.0001192071
I-
TOUGHNESS (IMPACT STRENGTH)
APPROPRIATE STIFFNESS
WEATHERABILITY AS NEEDED
I
APPEARANCE: SMOOTHNESS, GLOSS, AND COLOR
OTHER: CHEMICAL RESISTANCE, ETC.
r p+* H- -
.|.i
VAB.0001192072
Decision - which MW?
Limitations -
c
-fid I'..............
VAB.0001192073
RPVC Stabilizer Selection
A
CaZn weak stabilizer. In past used only where very low toxicity & odor needed. May replace much Pb and BaCd in European RPVC.
Vast majority of RPVC in USA is Sn stabilized. Good balance of properties.
Sb generally similar to Sn but less effective. Minor.
fr
ihlrri.
1 1 t
lI
**l' 1 '
Hv
+- -l-
VAB.0001192074
PVC Degradation Causes:
HC| generation Color Change Melt viscosity increases
(cross-linking) I Physical properties change
Therefore, stabilizers affect processing and end-use properties.
Essential additive
T I IT
.... ........................ *- J.ur;
: ,M.W m*.
'1^- >-
W*- ' I
,
r.|
VAB.0001192075
V
I 1
I Function- Assist processing:
I
Reduce melt viscosity and shear Boost thermal stability (often indirectly). Provide metal release Control fusion
Use is mandatory.
Types (theoretical) - Internal
Calcium Stearate
Generally use 2 or more lubricants in combination.
i %
> h
'I I
1 '"
11'll . T
A
Internal lubricants - not frequently used reduce melt viscosity only
External lubricants - generally retard fusion - provide metal release reduce melt viscosity "wax"
Calcium stearate - promote fusion reduce melt viscosity - costabilizer
VAB.0001192077
1 '*
B itf-nik
* -fc
A
i- r
VAB.0001192078
- :p.
IMPACT MODIFIERS
FUNCTION IMPROVE IMPACT STRENGTH MORE DUCTILE LESS BRITTLE
RUBBERY COPOLYMERS MAJOR TYPES
INTERIOR - MBS EXTERIOR - ABS
VAB.0001192079
>
*1i
il'i r' : M
'
^fK-
-Ij. '. H-r. - <1 : '-I1-
lL..piK>p . -
COLORING RIGID PVC
Color Concentrate: Pigment "Dispersed" In Carrier
Carrier Can Be:
Wax Liquid (E.G., Plasticizer)
Other Compatible Polymer (E.G., EVA)
Raw Pigment
VERSUS
Dispersion Problems
Messy
lgment Color Variations
Cheap
Flexible
Multi-Component
Requires Intensive Mixer
Fast Response
Color Concentrate "Some" Predispersion Less Cross-Contamination Uniform Color Expensive Inflexible Single Component Can Add On - Line Slower Matching
VAB.0001192080
1'
!*l *
it - : |
Functions
Reduce cost flbfooknne?)
Mgrhanhm Physical ChemicaBy inert re; PVC
rhmiigaii Times
Caidum carbonate (almost exclusively)
1 t tr
1 ii .......... r '
v
VAB.0001192081
< * "'i
,M
TYPICAL RIGII COMPOUND
r
PVC RESIN STABILIZER LUBRICANTS PROCESSING AID IMPACT MODIFIER FILLER PIGMENT
100 0.4 - 2.0 2.0 - 4.0
0 - 3.0 0 - 8.0 0 - 10.0 1.0 15.0
BASIS OF COMPOUND THERMAL STABILITY PROCESSING EASE PROCESSING EASE IMPACT STRENGTH COST REDUCTION COLORING
BALANCING PROPERTIES IS KEY
7 MECHANICAL PROPERTIES STIFFNESS / FLEXIBILITY TOUGHNESS USE TEMPERATURE RANGE
7 APPEARANCE
y FIRE RETARDANCY
y PROCESSABILITY
y CHEMICAL RESISTANCE
y INTERFACIAL PROPERTIES
y WEATHERABILIT Y
1 1>
N 11 r
i
VAB.0001192083
MANUFACTURE RIGID PVC
i ti .
'i--' -rt?r<p tc QHd r j -I
i.
VAB.0001192084
I l
OFTEN DETERMINED BY EQUIPMENT. SINGLE SCR6W8 FAVOR PELLETS,
ESPECIALLY NON-VENTED SINGLES. PELLETS ARE ALSO CLEANER:
LESS DUST & LEAKAGE.
DRYBLEND ADVANTAGES:
LOWER MANUFACTURING COST ONE LESS HEAT HISTORY (LOWER STABILIZER
COST OR HIGHER STABILITY) TWIN SCREWS WORK BETTER WITH DRYBLEND LESS OPPORTUNITY FOR COMPOUNDING VARIATIONS
T ' <'
'll
`
1 41.' -fWl I- . *r -t
..... H 11+ -J, ibr- . .,
VAB.00011 92085
BLENDING
HOMOGENEOUS MIXTURE
HIGH INTENSITY MIXING HIGH SPEED HIGH SHEAR HEATING
i
7 w-
' ' t
l ..................
r
14H** -
-- *
..i . h
" i
1I * sri . I *r
1air M
hhld-Ui. .
1 1i- . .
VAB.00011^2086
t
N
RESIN LUBRICANTS MODIFIERS COLORANT
MA8TER BATCH
BLENDER
VISTA DRYBLEND UNIT-ABERDEEN
MASTER BATCH USE BIN
BULK SILO
BOXING HOPPER
STABILIZER
FILLER RE9IN TI02
WELEX
QC 8AMPLE
'* 1 *
A h-*-'
-I
DI8CARD OVERS*
VAB.0001192087
COMMON TESTS
RIGID PVC COMPOUNDS
IZOD IMPACT HEAT DISTORTION TEST
TENSILE TEST
f n-i*
-t
t
I
VAB.00011 92089 3*
-k
taclli strength Is lbs maximum pulling load a nmtierlal can support before yielding or breaking.
? 1
E i'* r*-
1 1** *
' #--<
i u. q- .d h . j. ...
l --?- ,-m. ..
-K-rn rnvir-iKiii
.0001192090
Strain
Ttaulto iHm|Ui Is tN ualaf Uoaik bar.
1 IV
.. .j
VAB.0001192091
Pfelllag Dait Ibrt
laod lapaat Dut
1| l>.
-J k ,
h"-rJ, - sr
lb
s:
VAB.0001192092
lyptoi
Cor thla test
DjMtm
Quito
MIlUDait
MMlTflf
to Nwl NmUi| whoa struck os oiwfaoo
+ 1*. .. *- itp - H - + *
i -.i-- .
I
VAB.0001192093
#
Unnotchcd laod
Notched Izod
la ft/lbe per Inch.
1 . . . . . . . , . .. . . . . . . . .
H
.1| FIH
f ML .
VAB.0001192094
i 4-t
SF' "
t* -n
4H
VAB.0001192095
' i1
1'*
* If T
r.
r
1 I--.-
.'H. .
VAB.0001192096
--
1
APPLICATIONS
VISTEL TM
SPECIALTY PLUMBING FITTINGS VALVES TANK HOUSINGS
OUTDOOR PRODUCTS ELECTRICAL OUTLET BOXES RAIN GUTTER FITTINGS PATIO FURNITURE
GENERAL PURPOSE ELECTRIC BLANKET CONTROLS TELEPHONE JUNCTION BOXES
OTHER
rf 1 I
I
' - .................
-
fHM- h
L-: .
r I r V- '-
I
VAB.0001192097
END USE BENEFITS
VISTEL'"
INHERENT FLAME RETARDENT CHARACTERISTICS
EXCEPTIONAL PHYSICAL STRENGTH AND IMPACT RESISTANCE
GOOD STIFFNESS AND CREEP RESISTANCE
RELIABLE UV COLOR STABILITY AND WEATHERABILITY
EXCELLENT SURFACE APPEARANCE AND GLOSS
OUTSTANDING CHEMICAL RESISTANCE
Ll * v.
k
l|Tf-' . ->r h-
r
i
i
i
VAB.00011^2098
SUPREIT ENGINEERED
THERMOPLASTIC POLYMERS
SUPRELTM--
FAMILY OF COMPOUNDS
INCORPORATES PVC AS AN INGREDIENT
COMBINATION OF POLYMERS
VERY UNIQUE PROPERTIES
HDT IMPACT COLD TEMPERATURE PROCESSING LATITUDE
CUSTOM FORMULATED
VAB.00011^2100
*
PVC OVERVIEW
1I i
ri| inV i .;i p J;l
I
VAB.0001192101
i
TP
i
i l
. irt-H
ii-
i
i
)i
i
i
r
VAB.00011^2102
i
Polymers Research Group
v/Purpose of Polymers Research: develop new products improve existing products troubleshoot customer problems
y Approx. 35 in Austin R&D y 6 in Aberdeen plant
(Tech Service Lab)
PVC OVERVIEW
Polymers Research Group
Current Research
>/ PVC based polymeric blends & alloys (e.g. SuprelTM)
7 Recycling & waste minimization y Alternatives for heavy metal additives y Lower molecular weight resins
PVC OVERVIEW
Polymer Technology J. P. Kirkpatrick Diirector
Secretary V. G. Dougrey
b
H. J. Hail Senior Research
Associate
K. G. Mieure Development
Manager
Material R&D D. L. Wharry Research Manager
R. E. Asay C. D. Foshay M. D. Hein D. Mok E. V. Visneski J. Wallace C. P. Walters
Resin Technology H. G. Coleman
Sr. Group Leader R. C. Howe J. L. Irvine J. M. Janes
TESTING L. G. Clopton D. L. Ashley E. Marshall
1 M*
Safety/Environ R. B. Martin Supervisor
Technical Service R. D. Jackson
Research Manager S. R. Goodman J. E. Ingram J. V. Miller J. M. Quackenbush
Application Dev. S. H. Hookanson Research Manager
BETA G. A. Butler F. E. McAndrew B. A. Rushing M. M. Tannahill
WIRE/CABLE M. T. Corwin C. E. Hoover G. A. Jackson
4 ur
VAB.0001192105
t
HI |
,
Summary
Why PVC? low cost good physical, chemical,
weathering properties variety of processing techniques
PVC resin is not useable by itself
PVC Compound PVC Ream Other Ingredients Rigid Compound Flexible Compound
(has plasticizer)
Vista sells PVC Resin, Rigid & Flexible Compound
Customers who buy resin make compound themselves
PVC OVERVIEW
Summary
PVC Compound - two physical forms: Blend (powder) Rigid (dryblend) Flexible (Rotoflex Pellet Rigid (VistelTM F lex ible
Customers process Compound into final product:
Extrusion Injection Molding Calendering
Vista is... 6th largest Resin Largest Flexible Compound 4th largest Rigid Compound
...producer (by capacity, domestic)
PVC OVERVIEW
* It
V -i- i
s*
VAB.0001192107