Document 8Xm79oj5wgBQvLJvnRZBe1ay
GERMAN Literature on VC/PVC: MEASURES FOR HEALTH
2/24/75
________________________________________ PROTECTION
copies to (with TO/FROM note):
^^
Mr. R. C. Andrews Manager, Safety & Environmental Affairs Union Carbide Corporation 75 Stylon Road Wayne, New Jersey 07470
Mr. Wayne T. Brooks Director, Occupational Safety & Health Services Organization Resources Counselors, Inc, 1625 I Street, N.W. Washington, D. C. 20006
Mr. T. W. Carmody Mr. J. L. Carvajal
NY O'-21 514/ 82-3
Dr. Carl U. Dernehl
NY0-4
Mr. M, E. Eisenhour
Dr. D. H. Glenn Mr. R. E. Graebert
515/ 88
515/ 2 511/ 2000-3421
Mr. Don Guyette Union Carbide Corporation P. O. Box 698 Ottawa, Illinois 61350
Dr. R. W. Holland, Jr. Mr. H. V. Hooper, Jr. Dr. E. Q. Hull
Dr. W. R. Manning Mr. R. W. Martin
514/ 4 514/ 82-1 511/ 2000-3428
511/ 2000-3311 511/ 2000-4428
Mr. W. D. Neal
312/ 51 _
Dr. A. B. Steele Dr. T. T. Szabo
NYO -28 NYO -32
Mr. J. W. Whittlesey Mr. J. L. Worstell
NYO-46 514/ 406-2
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THE SOCIETY OF THE PLASTICS INDUSTRY. INC.
250 PARK AVENUE NEW YORK. NEW YORK 10017 12/573-9400
January 17, 1975
TO: Members of the VCM/PVC Producers Group
SUBJECT: German Literature on VC/PVC: MEASURES FOR HEAL1H PROTECTION
Attached Is a copy of a translation made available through the courtesy of Air Products and Chanlcals, Inc. This Is the literature that Dr. Ross Adams discussed at the December 6th meeting of the VCM/PVC Producers Group. It appears to give an up to date status on the German knowledge of this problem.
Respectfully,
JHL:Jo Attachment
John R. Lawrence Director of Technical Liaison
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VC/PVC: MEASURES FOR HEALTH PROTECTION Published By: German Society of Plastics Industry (VUE) 6 Frankfurt/Main Karlstrasse 21 Tclcnhane f06111 23 78 07/17
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TABLE OF CONTENTS
PVC-PRODUCTION Consumption Polymerization of VC
WORK RELATED MEDICAL PROBLEMS Maximum Concentration at the Place of Work First Indications of Cancer Threat Cases of Illness In West Germany Research Studies Emergency Measures Suspension of the MAK-Value Technical Standard Concentration for VC
RESIDUAL VC IN PVC Time Relationship Path of Diffusion Temperature Relationship
HEALTH PROTECTION IN PROCESSING AREAS Storing - Mixing - Extruding Injection Molding - Calendering - Paste Processing
VC CONTENT IN THE FINISHED PROOUCT
METHODS FOR THE MEASUREMENT OF VC Drager Capillary - FID-Method Ionoflux-Instruments - Ultrared Instruments Gas Chromatography - Sailing
VC-REDUCTION Present Reference Values Future Considerations
THIS IS PVC Manufacturing Properties
Page 2 4
12
17
*
21 25
29
33
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Vinyl Chloride (VC) Is feedstock for one of the most frequently used and most
versatile plastic materials.
Polyvinyl Chloride (PVC).
Recent scientific findings lead to the suspicion, that VC gas In certain concentrations has a carcinogenic effect.
Knowledge and suspicions which In this connection have been accumulated over approximately 1 year are news tcjsclence as well as regulatory authorities and the
Industry worldwide.
This pamphlet attempts to explain the present state of knowledge and findings. In addition we would like to point out directions for safety measures which have to be followed In the plastics Industry.
It Is possible that new evidences have been accumulated since this pamphlet has.
gone to printing.
*
Waiting for these, however, Is not feasible. We are primarily concerned to convey the understanding of this problem not only to the PVC processing Industry but to larger areas of the public.
Dated: Frankfurt/November 12, 1974
-1-
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PVC-PRODUCTION
PVC has been manufactured In the Federal Republic for over 30 years.
Consumption
Production for 1973 was 1(034t000 metric tons with a value of approximately 1 BillIon(German marks)DM. PVC Is used In almost all areas of the econony whereby primary Industries such as the construction business, electrical Industry and the automotive Industry ere particularly heavily dependent on this plastic material.
PVC-Consumptlon 1973 Pipe and Fittings Flooring Cable Installations Films (Flexible and Rigid) Profiles,Including Windows Coated Fabrics (Artificial Leather) Venetian Blinds, Building Tiles, Fascia Bottles Ribbons, Strings, Ropes Hose Records, Shoes, Driving Belts, Conveyor Belts, Foam Materials Total
% 23 10 11 22
9 4 6 2 2 2
9
100
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Polymerization of VC
PVC Is commercially manufactured In the Federal Republic by three different methods:
Emulslons-Polymerlzatlon Suspensions-Polymerization Buik-Polymerlzatlon
Polymerization of Vinyl Chloride to Polyvinyl Chloride Is conducted at tempera tures between 40 and 80C at a VC vapor pressure of approximately 6 to 14 atmospheres. At atmospheric pressure.Vinyl Chloride has a boiling point of minus 13C and during polymerlzatlon^ls dissolved In significant amounts In the produced PVC Vihese dissolved quantities are converted Into PVC to a large degree,as the polymerization process progresses.
The speed of any chemical reaction depends on the concentration of the used
raw materials. Consequently polymerization of VC to PVC Is slowed
toward
the end of the reaction since the concentration of the monomeric VC In the
reaction mixture Is constantly decreased. Theoretically It would take forever
to await
polymerization of the residual VC. Hence the reaction Is stopped
depending on the process used, after approximately 90S of the VC has been
polymerized. The point In time at which the reaction Is stopped Is essential
for the properties which are desired and necessary for further processing.
In all processes termination Is achieved by evacuation of the residual VC
gas from the autoclave. It Is recovered by llqulfactlon and Is recycled to
the production process.
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Economic reasons dictate a recovery as complete as possible since It Is sub
stantially more difficult to recover VC gas which escapes during further
processing steps such as drying* classifying and movement wfthln the plant.
In spite of a massive amount of technical efforts* the removal of VC gas as
present In small amounts In PVC particles has been unsuccessful to date.
This Is difficult to conprehend In recognition of the fact that Vinyl Chloride
bolls at minus 13C and Is temporarily exposed to temperatures up to 250C ^understood to bey
during the drying process. The reason for this Is
'V as follows:
The liberation of monomer which Is dissolved In PVC occurs on the surface of V(m1grates)7
the Individual PVC particle, on to which It dlffusesjfroci the Inside. This
diffusion process Is defined by the drop In concentration toward the surface,
the length of the diffusion path and above all by the temperature.
WORK RELATED MEDICAL PROBLEMS
(as early as the 1930`s when thej
A narcotic effect upon Inhalation of VC had been recognized
$ large
scale use of VC
had reached significant proportions.
Not until the beginning of the 1960's did scientists discover
diseases such as acroosteolysls, scleroderma and liver diseases.
Maximum Concentration At the Place of Work
A coomlttee of the German Research Association (DFG) specifies maximum exposure levels (MAK) for purposes of health protection In production operations for VC as well as for many other chemicals.
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In 1966 a MAK value of 500 ppm had been specified In Germany. The comnlttee for testing of hazardous materials of the German Research Association defines the MAK value as the concentration of a gas, vapor or particle suspended In air at the place of work, whlch.based on present knowledge,does not Impair the health of the worker under repetitive and long lasting exposure usually
vper7 8 hours per day, however, not to exceed 45 hours* average work week.
Studies by the American professor T. R. Torkelson ^, led to the reduction
of the HAK value to 100 ppm after he discovered hlstopathologlcal liver alterations In his animal tests with rats exposed to 200 ppm during a period of 6 months.
Yet the reference book "Chemistry and Toxicology of Plastic Materials" explained as late as 1970: "Vinyl Chloride Is a gas with relatively low toxicity. In higher concentrations It has a slightly anesthetic effect and causes Irritation of the eyes."
First Indications of Cancer Threat
^evidence; ' Investigations known until then had not produced any " ^ of a possible cancer
threat by Vinyl Chloride. The connection between Vinyl Chloride and a cancer
vas recentlyy
I
xhasv
threat ^
treated Infrequent discussions,* been documented In studies
by Professor Viola ^ for the first time In 1970. His tests with rats
ywerey however,^conducted at unrealistically high doses, which up to 30,000 ppm
bordered on the explosion limit of a VC/air mixture.1 2
1) American Industrial Hygiene Association, Journal Volume 22, Page 354 2) Presentation, 10th International Cancer Congress, 22-29 of Hay 1970,
Houston, Texas
-5-
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Professor Maltonl of the Oncological Institute* Bologna* Italy was commissioned
an by International group of companies to explore In depth the effects of YC
under actual operating
conditions. Preliminary reports Issued In the
sunmer of 1974 show that rats which had been exposed up to 1 year to a range of VC
yfrom j concentrations * more than 200 to
as low as 50 ppm. have contracted
angiosarcoma
of the liver* a special cancer of the liver.
*R1n-Test> In the U.S. y Laboratories In North Brook* Illinois detected almost
simultaneously the same liver damages In mice after 7 months exposure to
50 ppm VC. As an emergency measure the use of VC as propellant In aersol
sprays was prohibited In the United States and stopped In West Germany.
Cases of Illness In West Germany
Professor G. Veltman of the University Clinic for Skin Diseases* Bonn* West Germany had previously determined the danger of VC to the human body on workers which had been employed In PVC production. As a result In recognition of loportant discoveries In the area of Industrial medicine and worker protection* he and his co-workers received the Franz Koelsch Reward
^Manufacturers Association^ donated by the Tp2 of the Chemical Industry*
Through the end of August 1974 a total of 124 suspected cases of the *so-
calledTcrfsease" had been reported by a few PVC producers In the Federal
\Soc1al Security/
Republic^ ^
Insurance carriers have recognized 43 of these cases
as occupational diseases.
^definition,/ The medical " ^ of these 43 recognized cases are primarily specified as
Raynaud's Syndrome* liver and spleen damages* thrombocytolysls and retlculocytosls.
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41 of the afflicted persons have In the meantime resumed employment.
Professor Veltman's studies revealed that,1n the severe cases a change had
been diagnosed In lung, liver, spleen, skin and vascular systems. Hls.as
well as simultaneously publicized studies In other countries gave the signal
for a retroactive Investigation of the causes for the death of workers previously
enployed In VC and PVC production. Three cases of. hemangloendothellosarcoma IhayeV
of the liver, a very rarne case of cancer, V been diagnosed In this connection
In the Federal Republic:
A worker,who died at the age of 38 and who was employed from 1956 through 1968 e.g. 12 years In a PVC production plant, last as polymerlzer scrubber.
A chemical worker who who died at the age of 39.
lhad been employedJ for 11 yearskln a PVC producing plant and
An operator who was employed In the filling of aerosol spray cans In which
VC had been added as a propellant. He had been exposed to VC a minimum of
Enlargement of the spleenJ
14 years and died at the age of 43. A. liver fibrosis with""
^
and esophageal varlcosls had been diagnosed during his lifetime.
Vbetween thesej Studies to determine the extent of correlation 'F Heaths and VC In these
plants are still under Investigation.
Hence It Is too early to finalize a conclusion on the extent of the existence
of this disease. The examination of the causes for death are rendered more
difficult as a post diagnosis does not lead to reliable results, and *s to
date angiosarcoma
has been found only after more then 10 years
exposure.
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Research Studies
In addition,to date there Is no unequivocal proof that the occurred symptoms of
lexcluslvelyj
disease can be attrlbuted^to the
Influence of VC. In view of this
the Ministry for Work and Social Order has commissioned a research project UmpurltlesJ
to clarify If process related 4^ In VC could be considered as cause
for the disease.
ibelngy Further research projects for the elucidation of the VC disease are+conducted
Ithej
In cooperation betweentProfess1onal Trade Organization of the Chemical
Industry, the Federal Ministry for Work and Social Order and
the State
Government of Nordrhein-Westfalen. Participants are: Professor Or. Henschler,
Institute for Toxicology and Pharmacology, University of WUrzburg, Professor
Or. Lehnert, Central Institute for Industrial Medicine, University Hamburg, UndustryJ
and the State Physician for-Tor Nordrhein-Westfalen, Dr. Relnl, Ousseldorf.
In particular these studies Include the effects of VC on the human organism
(Investigations of metabolism), the compilation of a literature survey and
evaluations^ well as epidemiological Investigations (determination of Illness
/lby differentiated group comparison),/
risk factors
'4'"
The Central Institute for
Ifood Research/ In Zelst, Holland was commissioned by the Society of the Plastics
Industry and PVC producers In Holland to conduct a 90 day feed test to deter
mine the oral toxicity of VC In rats with ratios of 0, 30, 100 and 300 mg
VCper kilogram body weight. At a ratio of 30 mg VC per kilogram body weight,
these studies resulted In a "dosage without effects". 100*and 300 mg VC
Vresult inJ per kilogram did not ^"concentrations with direct toxic effects."
Further Information Is expected as a result of a follow-up 2 year test for
the determination of objectionable VC concentrations.
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Emergency Measures
After recognition of these problems It Mould have been Irresponsible to await results from further long term studies. Emergency measures for the reduction of risk at the place of work In PVC producing plants where hence applied as deemed necessary. This 1$ reported In Document 7/1627 of the House of Representatives by the State Secretary of the Ministry for Work and Social Order on January 29, 1974 In response to an Inquiry by a State Representative. Guidelines for safety measures to prevent Injuries due to handling a Vinyl Chloride were significantly tighten In April 1974 In cooperation between the Trade Union of the Chemical Industry and specialist. the plastics producing industry. Addltlonallyvcontlnuous observations of employees were Introduced In cooperation
tfromj between Trade Union and experts A/ the Industry In Industrial medicine over and above the ongoing preventive medical examinations. They are documented In the July 1974 Issue of "Principles for Preventive Industrial Medical Examinations" by the Trade Union.
Suspension of the MAK Value
A reduction of the established MAK values has been Investigated In connection with the Introduction of a variety of measures. In this connection the Comnlsslon for the Investigation of Health Hazardous Materials had to consider, that the handling of potentially carcinogenic materials require special safety measures and precautions In health protection. Such materials have
ipubllshedj therefore for some time been eliminated from thetlist of MAK values and have been reported separately. VC has been added to the list of carcinogenic
ithey materials In view of the results fromjanlmal experiments and the experienced
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cases of Illness. The previously established MAK value was suspended. The Commission for the Investigation of Health Hazardous
Materials Issued a related statement dated June 14, 1974:
VpotentlallyJ
"The handling of proven or
carcinogenic materials requires
special precautions and measures for health protection. Hence these are
Specifically enumerated and classified as those which
a) can cause severe tumors as experienced In human beings
b) so far have only been Investigated by animal tests under cond1tion$,wh1ch
are comparable to
possible exposure of hunan beings In the work
process and which In the opinion of the Connrisslon have definitely
proven to be carcinogenic:
e.g. Vinyl Chloride
^containing; ^amounts of) Iwasi Vinyl Chloride only minor^impurities definitely carcinogenic by animal tests. A special type of liver tumor (hemangloendothellosarcoma) has been observed with workers which had been exposed to high Vinyl Chloride concentrations In specific work locations In the PVC producing Industry. A causal correlation Is 1mn1nent,at this stage, however, nonproven. It
remains to be seen whether the recently Introduced In depth toxicological Investigations as well as the retrospective stipulations with regards to employees' contact with Vinyl Chloride confirm or Invalidate this relationship."
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Technical Standard Concentration for VC
A so called "Technical Standard Concentration (TRK),M akin to that established
for benzene. Is to be established following the suspension of the MAK
value by a Committee for Dangerous Materials (AgA) organized
by the
Ministry for Work and Social Order which Is composed of representative experts
from trade union and Industry. This standard Is defined as follows:
"Compliance with the Technical Standard Concentration at the place of work
should reduce the risk of a health hazard, Is however unable to completely
eliminate this risk. The Technical Standard Concentration Is based on
technical circumstances and
possibilities of the technical prophylaxis
Un conjunction withy
^
work related medical experiences In
handling dangerous
materials. Compliance with the Technical Standard Concentration does not
completely eliminate the risk of Impairment of health; hence by continuing
Improvements of the technical circumstances and the technical Ifor protection.)
measures Vconcentrations have to be aspired which fall as far below .the Tech
nical Standard Concentration as possible." ^
Up until the suspension
of the MAK value for VC. according to a release
by the Federal Ministry for Work and Social Order of May 22, 1974, a 50 ppm ^adopted]
level was + as recoumended by the Trade Union of the Chemical Industy. The
soon to be released Technical Standard Concentration Is expected to be
lower. The continuous analytical monitoring of such low VC concentrations
Vplace atmospherej
In the work^ Is expensive. Hence It Is Imperative that producers and
^processors!
kwlthj
5 of PVC familiarize themselvestand work toward Integration of the
expected parameters.
1) Work Protection Issue #5/1974, Page 170 -11-
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A program of regular medical examinations of the employees Is already self* \theseJ
evident. The work safety law requires ^ for all Industrial areas starting
January 1, 1975.
RESIDUAL VC IN PVC
Polymerized PVC contains a residual amount of VC based on production related
technical parameters as explained above. Depending on Its viscosity, particle Vs1ze7
size and part1credistribution,as well as ambient temperature this residual
VC migrates to varying degrees to the ambient
atmosphere.
An exponentially declining curve results If the residual VC contents are
plotted over time.
This
Vjrlth porous 7
curve has a steeper slope than with dense products and Its slope Increases also
with Increasing temperatures. The possibility for the lowering of the residual
amount of VC In PVC are defined by-time,
- path of diffusion,
Time Relationship
- temperature.
(customary allowance) (diffusionj
The hereto $
for gas
3/ would have to be extended significantly
to days or even weeks - In order to achieve a significant reduction in the
residual VC content. An extended residence time In dryers or tiegassing equipment
\.used 7
under presently
temperature conditions would damage
PVC by thermal
\whlch would bey
degradation not to mention the warehousing problems^caused by such measures.
A temperature reduction during degassing on the other hand would mean a further (Installations 7
prolongation of the process. Specially equipped degassing ^ tdurlngy
would have
to be constructed*
Adopting appropriate measures ^ compounding seems
a more reasonable approach today.
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VC-Content (ppm) log. scale
Dense Particle Porous Particle Days Abatement of Residual VC In PVC During Storage In Bags The two curves show the development for two types of PVC with approximate Ivlscoslties J equal ^ whereby the curve with the flat slope represents (while; a relatively dense particle * the other curve represents a porous particle.
uce
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<.n
Path of Diffusion The length of the path of diffusion during degassing depends on
- the particle size, the larger the particle the longer the path of diffusion.
- the particle density, e.g. porosity and porosity characteristic. The more pronounced the porosity or specific surface area, the shorter Is the diffusion path.
La variety of end products j
Production of
and the application o
processing
techniques would be Impossible If PVC were exclusively produced to obtain Vpurposes.)
optimum particle properties for degassing ^ The market requires PVC properties
ranging from the finest to the coarsest and from the most porous to the gel
particle. The viscosity of PVC
a function of
polymerl-
zatlon temperature also influences Its porosity. The higher the .polymerization
temperature,the lower the viscosity and the denser the particle.
Temperature Relationship
Degassing of PVC Is accelerated with Increasing temperature. Limiting, however.
Is the thermal stability of PVC. The addition of stabilizers at this stage
Is hardly suitable since the scope of application for the product would
be significantly reduced. Hence commercial PVC
contalnsfcertain
amount of residual VC. have to be taken
it follows that preventive measures
Las welly In the area of processing^h order to prevent a
health hazard by VC volatility.
-14
Abnahmc des VC-Gehalts in Abhlnglgkeit von dor Lagerzeit (Beispiel 2)
Reduction of VC-Content as a result of warehousing time
PVC 1600 ppm VC
I wenige
yTage
\/
| Sack lagerung
570 ppm VC
Marehousing for several days In bags
Days
ITag 3Tage 5Tage 8Tage
\Z "\ 210 ppm VC
110 ppm VC SO ppm VC
in
Softener Schale
10 ppm VC
In open cup
Modellversuch mit einem PVCMuster von extrcm hohem VC-Gehalt. Boi hoher Temperatur und Vakuum sinkt der VC-Gehalt in wenlgen Minuten auf Brucbteile des ursprungiichen Werles txlt
(Beispiel 3)
Small scale test on PVC with extremely high VCContent
Under high temperatures and vacuum,VC-Content drops In a few minutes to a fraction of the original level
PVC 6000 ppm VC
I 1120*C.
^200Torr
\/
I 55 min.
40 ppm VC im Compound
200 nm Hg. In coirpound
\/
35 ppm VC in der Flaschenwandung
In blown bottle wall
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HEALTH PROTECTION IN PROCESSING AREAS
We therefore present here some Ideas on how to avoid accumulation of VC In the work area atmosphere.
Storing
No special precautions are necessary for storing In silos, with the exception of access during maintenance and cleaning operations. Ample ventilation on the other hand should be provided In storage areas for bagged material In order to
vexcessive; prevent accumulation of \ VC concentrations.
Mixing
Most processing methods which do not require pellets or ready made compounds vmlxers.)
are preceded by mixing operations. Intensive ^ as used today and partic ularly the application of higher temperatures,stimulate and accelerate the liberation of residual VC from PVC thereby eliminating the major portion of the monomer. On one hand this presents an advantage as PVC processed In such a manner contains but traces of VC. On the other hand, however. It necessi tates safety measures for mixing areas and equipment.
yclrcumstanceJ Up to several hundred ppm VC have been detected at mixer openings. Under any ^ this Is significantly higher than the pending standard levels. It Is therefore Imperative that these mixers are not vented toward the general plant area. The processing sequence of silo*mixer, cooler, processing equipment should for the same reason operate as a closed system with ventilation toward the outside. VC concentration In the mixing area can be held under 10 ppm by these measures.
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Residual VC contents In relation to processing temperatures
on a sample with particularly high VC content.
PVC in the. Intensive
mixer.
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In general terms hot mixing entails advantages,since significantly larger Idurlng J
proportions of VC are driven off than ^ cold mixing as shown In the following
examples. This ensures that none or only very small amounts of VC are released
In further processing steps.
Extruding
IconflrmedJ
A variety of tests ' ^ that the evaporation of VC from PVC Is significantly'
UlsoV
Impaired after thermoplastic conversion Into finished products. ThlsTapplIes
yprocessingy
to the hot melt
as It emerges from >J/ equip-
ment. Indicative Is the measurement of a 10 ppm VC level obtained directly ^Specialj
at the exit of a large scale granulator.^ precautlons have to be taken
at the hopper when processing powder b1ends,as heating accelerates
the VC degasification. The recommendation goes to provide for sufficient
ventilation at this point or even better to operate an enclosed system.
Injection Molding
Monitoring the VC concentration In the vicinity of Injection molding machines both In the Federal Republic as well as In Great Britain showed also a level under 10 ppm. Recoamendatlons made for extrusion processing apply here as well.
Calendering
In the calendering process attention should be concentrated on the Initial yequlpmentj
processing steps. Mixing as well as preplastlf1catlon^have to be equipped
with sufficient ventilation.
Work areas around
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Abnahme des vOGehau* in Abhingigkeit von don Vorarboitungs*
Decrease In VC-Content In relation to processing conditions
bedingungen (Belsplel 5)
pvc
600 ppm VC
cold premixing and g? anulated
ykail vorgemischt A120*C.5mia,200Torr?
undgranuliert \Compoundierung
V
220 ppm VC
im Granuiat In Granulate
10 ppm'VC im compound
Compounding in Compound
0
95 ppm VC In dor Flaschenwandung
10 ppm VC in dor Flaschenwandung
In blown bottle wall
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031582
processing equipment are relatively free of
VC exposure as
Vyentllatlony
calenders
are already equipped with adequate T
units for the
elimination of plasticizer and additive fumes.
Paste Processing
Only minute traces of VC are liberated during processing of paste formulations
from emulsion PVC at room temperature. This Is primarily attributable to
the fact that emulsion PVC has the lowest residual VC content of all three
lventilation)
types of PVC. Typically,Installed ^
apparatuses which serve to
eliminate
plasticizer fumes during the curing step
are
satisfactory to eliminate traces of VC as well. Mandatory Incineration equip
ment, which Is required for the elimination of organic vapors at these large
scale processing Installations*provides an additional safety measure.
VC CONTENT IN THE FINISHED PRODUCT
Up until two years ago It was generally accepted that monomeric Vinyl Chloride gas would have evaporated completely by the time It reached the thermoplastic processing step and that consequently finished parts were free of monomer. This perception provided the basis for regulations as established by health authorities In many countries. Similarly In the U.S.A. PVC was classified In a group of materials generally considered as nontoxic with the designation of "prior sanctioned material."
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Beim Kaltmischcn blcibt der VCGehalt unvcrandert. AnschlloOondcs Kalandricron 1st hinsichtlich dor
VC-Content remains unchanged by cold mixing. Subsequent calendering Is not very effective
In the reduction of VC.
VC-Roduzierung nicht sohr otfoktiv
1 (Beispiel 6)
PVC 300 ppm VC
\/
300 ppm VC
kalt gemischt
Cold Mixing
kalandriert
\/ J
160 ppm VC in 250 n Folio
Calendered in 0.25 nn Film
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031584
tv.
In the spring of 1974 reports from the U.S.A. Indicated that a 20 ppm VC
content had been found In whiskey which was contained In PVC bottles. Subse
quently the Food and Drug Administration prohibited the packaging of alcoholic Ito date;
beverages In PVC bottles. In spite of concentrated effortsfro further infor
mation could be obtained with regards to the PVC or the tused in this Instance In the U.S.A.7
analytical methods i'The following Investigations were conducted In
Germany In order to clarify the circumstances:
Development of more accurate and Improvement of known analytical methods.
Investigation of VC migration Into food products from consumer products such as packaging materials.
Investigation of the Impact of processing characteristics on the VC
concentration In
consumer product
Representative food products and storing conditions such as stipulated In the recommendations for consumer products by the Federal Health Administration were used for the Investigation of the migration of VC from PVC packaging materials. The following representative food products were used: water, 302 concentration of acetic acid, IDS concentration of alcohol and edible oil. They were stored In PVC bottles for 10 days at 40C, which at room temperature corresponds to a time period of several months. 40% and 50% alcohol concentrations were Included In order to verify the surprising results as reported In the U.S.A.
lhad] The applied analytical methods^ a minimum detection level of 0.2 ppm with the solutions In water and 1 ppm with edible oil.
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Test results were generally below or In the vicinity of the minimum detection
level even with relatively high VC concentrations In the bottle wall and hence Usj
fell significantly below the 20 ppm VCVdetected In the U.S.A.
The Commission for Plastic Materials of the Federal Health Administration ^produced)
comnents on the "examination of consumer products$ from PVC according
to the latest state of scientific knowledge":
"The Comnlsslon for Plastic Materials of the Federal Health Administration
reports In Its 57th Sesslon.that to date there are no Indications of a health
hazard by consumption of food products which had been packaged In PVC.
Experimental 90 day animal tests had been concluded In September 1974 by the
Dutch Central Institute for Food Research during which substantially higher
Ithan those)
amounts of VC had been administered ^
which could possibly be expected
as a result of contact of PVC with food products. There were no Indications
of a toxic effect. In view of this the oral Intake of traces of VC with food
products has to be treated In a different way then the Intake of VC by In
halation.
Analytical tests on a broad range of food products which were packaged in
commercial PVC resulted exclusively In levels below 1 ppm VC (e.g. less than
(VC per kq.ofy 1 mg*food product). These tests are presently continued on a broader scope.
Based on
animal testing and analytical results the Commission for Plastic
(as a precautionary measure
Materials of the Federal Health Administration has no reservations 1t+tfie VC
content In food products Is
limited to 1 ppm until new evidence
is presented as a result of the conmlssloned long range tests.
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The Federal Health Administration expects that all technological possibilities for a reduction of the VC content In the production of PVC materials as well as In Its conversion to consumer products will be adopted.1*
The Food and Drug Administration In the U.S.A. to date has considered a
limitation of the VC content to 10 ppm In finished products which are destined
for contact with food products; according to the latest Information, however.
It Is expected that the FDA Is working toward an arrangement with which the lable toy
Industry is presently^comply. The FDA has not arrived at a decision yet
whether to Impose a VC limitation In the finished product or
In
food products or respectively In representative test media and what the
level of such limitations should be.
METHODS FOR MEASUREMENT OF VC
Vbey Refined methods have tovapplled and highly sensitive Instruments have to be used for the control of VC concentrations In the ppm range. This applies to
monitoring of work place conditions In PVC producing and processing plants as well as to securing the consumer protection In PVC packaging of food products and to the determination of the residual monomer In PVC.
N
Draper Capillary
Until now the detection level of the most simple and economical method for
thasJ
the determination of VC In altysufflced: the analysis by the "Drager
Capillary Vinyl Chloride 100/a," In which air Is being sucked through the
capillary with a hand pump. If after 40 strokes the color of the capillary
Is unchanged, then the VC level In the air lies below 50 ppm. It can hardly
ucc
031587
be expected, however, that this detection limit will suffice for plant
tt monitoring purposes. The Drager Capillary will, however, retain Its signif
icance In a quick spot analysis,particularly since It has a relatively high vwhich serves as Indicator J
reliability. Reaction with Potassium Permanganateloccurs aside from
Vinyl Chloride only with a limited number of other mostly unsaturated organic
compounds such as ethylene or chloroprene. These should however resent)
rarely^in conjunction with VC.
only
FID-Method
A significantly more sensitive method, which dependent on Instrument design
Ifor) can be applled^^spot or
constant monitoring In exhaust ducts,capitalizes
on the fact that during Incineration of organic substances In a hydrogen-
mlxture,
air-
Ions are created which significantly Increase the electrical con-
(Instrument^
ductlvlty. Inside such a FID
(flame Ionization detector) the flame
ywlthin I
bums ^ an electrical field which Is created between the torch nozzle
lfounter>>
and aH' electrode by the application of approximately 200 volts. The
resulting Ions move In this field, - the resulting amperage is approximately
proportional to the amount of the Introduced organically bound carbon. The ^conceivably J
detection level of the FID could V Be lower than 1 ppm. If Its selec
tivity would permit this. It responds practically to all organic compounds, \only known/
such thabjcondltlons In existence at the test location
would allow a judgement as to what substance caused the signal. At low
concentrations
this naturally Is always an uncertainty. Advantageous Is its
fast response of approximately 1 second which allows
rapid and successive
monitoring of several locations.
ucc
031588 -26-
Ionoflux-Instrument
lonoflux Instruments work also on a continuous basis, however with higher
selectivity. Here the Increase In
electrical conductivity of atlabsorptlon
solution,which Is proportionate to the VC content,Is being measured. Initially
the VC Is burned with a catalyst whereby hydrogen chloride and chlorine are derived
from chemically bound chlorine. Subsequently both gases are absorbed In a
hydroxylamine solution, whereby the chlorine Is converted to hydrogen chloride.
The Increasing conductivity caused by the total amount of hydrogen chloride
corresponds exactly to the Introduced amount of VC. These reactions require
a certain amount of time, such that an Indication of the VC content does not
show until 5 minutes after dosage. The detection limit of this method Is
1 ppm.
Ultrared Instruments ^
Ultrared instruments represent an effort to Improve the selectivity on the
4
scale of trace concentrations. Two types can be distinguished: the Uras-type Vwhlch usesj
which does not work dispersive bufclrthe test gas as reference gas and
those Instruments which operate dispersive with prisms and filters.
Gas-Chromatography
The highest degree of selectlvltyVachleved by gas chromatography which, however,
can only measure
IThls method V
i ..
continuously/ ^ tbfaolnes the advantagejbf selectivity
with high accuracy and sensitivity. Here the flame Ionization detector
Is hooked up with a coupling unit which allows the classification of the test
specimen by boiling point and affinity of Its components. These are Intro
duced one by one by means of the carrier gas Into the detector which analyses
1) Translator's Note: Infrared (?) -27-
ucc 031589
them quantitatively, from exhaust ducts.
Samples can be taken from any areas or extracted
Detection Limit and Selectivity of Various Methods for the Determination of Vinyl Chloride in Air
Instrument
Detection Limit (ppm Volume)
Selectivity
Interference Factors
M
Drager Capillary
50
Limited
Unsaturated hydrocarbons
FID
1
None
All Hydrocarbons
and Ammonium
Ionoflux Type
1
Slightly
Halogenated
Limited
hydrocarbons
Ultrared (Uras-type)
Ultrared (Dispersive)
5 Dusts,
Limited
Vapors,
Carbon Dioxide 0.7
GasChromatography
0.2
Available
Minimal
W VC contents In food products and In PVC can be defined Inrslmilar fashion.
Food products such as mineral water, wine vinegar or alcoholic beverages, as
^hypodermic,/
well as molten fats and oils are Introduced with a
needle In the
dosage section which Is heated to 100C, whereby volatile portions evaporate
ucc
28- 031590
Immediately and are carried away by the carrier gas.
For testing of PVC, a solid which can not be Injected, a solution of the
isuch as in tetrahydrofuran j
polymer^is required asa first step.
Obtainable
detection limits for VC are 0.2 ppm In air (volume ratio),^ 0.2 ppm (weight
ratio) In water and fat based food products and 1 to 5 ppm (weight ratio) for PVC.
Sampling
Correct sampling Is very Important.
Sample size must be large
enough to show a representative cross section of the total. The usual methods
Iblendlng.y
to obtain
such an average sample Include ^ dividing, homog
enizing and the like. In the case of PVC in powder form It has to be recognized
lvolatilize;
that particles which lie near the surface
`"faster than those which are
located in the center of the bulk.
VC-REDUCTION
land flashing;
Residual monomer which after polymerlzatlon^remalned In the PVC
(to a large extent IntoJ
typically volatilizes
i
tfie atmosphere during
drying, classifying and air conveying operations*
The
Intensive efforts by the industry to operate
at low emission and
1) PPM (volume ratio) and (weight ratios) differ In the determination of
Vinyl Chloride traces in air numerically by a factor of 2.6. PPM (volume
vvoTumey
J
ratio) represents
tne^rUllo
of Vinyl Chloride gas to
total gas
PPM (weight ratio) on the other hand Is the weight
portion of Vinyl Chloride of the total weight. The density of Vinyl
Chloride gas Is approximately twice that of air. -29-
uce 031591
^volatilization)
loss levels concentrate on achieving a radical^
method applied to a
system which Is hermetically closed to the ambient atmosphere, and which is
expected to further lower the VC content In commercial PVC.
The administrative regulations for the Environmental Protection Law - the so
called"Techn1cal Direction Air"- Imposes a strong restriction on VC contamination vyc/
allowed to the environment with a maximum of 150 mgfper m Ivolume j exhaust^with a flow rate of 3 kg per hour.
In view of the measures to be taken at all processing operations, knowing the
concentration
^commercialJ
of VC in the various types of sf PVC should receive considerable
attention. These VC contents are presently still to be used as guidelines
for the protection of the worker In ` processing areas. It is self-evident,
however, that this can only be a temporary stop gap measure. By consensus
among PVC producers,the solution to the VC problem can only be achieved through a
ithe i
icommercial PVCJ
drastic lowering of4VC content in
J
or compound.
Present Reference Values An opinion on the
(content as experienced todayJ residual VC Sr has to remain very vague, however,
unless It refers to specific types of PVC. Nevertheless some guideline
values shall be given as follows:
With emulsion PVC a significant factor Is whether it Is a fine or coarse grain
type. Finely sprayed emulsion PVC
contains a maximum of 10 ppm VC, a
typically level Is 2 to 7 ppm. Coarsely sprayed emulsion PVC generally contains
150 to 200, maximum approximately 250 ppm. Special grades such as used for
ucc
-30- 031592
la maximum level of} paste formulations containfapproxlmately 70 ppm,typically
however,around 20 ppm VC.
f
The range of applications for suspension PVC Is much larger than that for the
other two types of PVC. Correspondingly many different grades of suspension
PVC are being produced to satisfy market demands. General comnents on
Vsingle J the VC content are difficult, as there Is no correlation to any ^ property.
Icategorlcally I An attempt toireduce tne VC content
leads to a change
In the overall properties of PVC.
Therefore only close
cooperation between processor and producer makes the attainment of a
minimum
VC content possible with a simultaneous maintenance of
ylt follows, that,;
property differences.
^ presently only a range of VC content between
yfor j
^postulated.}
10 to 1,000 ppm ^ suspension type PVC can be V These values could be
can
higher for specialty types. The supplier provide pertinent Information.
Typically
residual VC contents for bulk PVC fall In the range of
Vspeaking,J
100 to 1,000 ppm. Bulk PVC degasses particularly quickly. Therefore, generally ^
VC contents are significantly lower at the processor level.
(alone } These broad Indications^show
content Is simply Impossible.
that a general statement on the monomer
Imakesy The required differentiation % a direct
dialogue for the determination of exact levels between producer and processor
Indispensable.
In additlory the above Indicated residual VC contents have resulted from testing of freshly produced PVC. Further degassing occurs during the various shipping steps and storage In bags or silos. It Is therefore Impossible to make binding
ucc
-31- 031593
statements on the residual amount of VC In existence at the time of delivery to the processor. Only maximum values could possibly be Indicated.
Likewise at PVC producer can not guarantee a specific minimum storage time with corresponding VC reduction. The reason for this Is,that all PVC producers maintain a lower number of production lines than the number of grades they offer. Several grades are therefore successively produced on one line. It follows that production has to be In large lots and shipments have to be equalized over constantly and significantly changing Inventory levels. As
Un conjunction withy a consequence the shipment of a mixture of freshly produced ^ already several weeks aged PVC Is unavoidable.
Future Considerations Vare undertaking/
All PVC producers ^ intensive efforts to develop new processes which in
spite of technological difficulties will allow a further,significant reduction
of residual VC contents.
Pilot plant know-how Is already available. icomnerclal j
seal1ng up to^PVC production quantities.
V,being J
Much work Is presently^done In
Design, ordering, delivery and Installation of new equipment require time however.
Finally, as experience shows, time Is also required for a legislative examination and approval of new processes.
Overall, there Is no doubt, that In
time we will be successful In upgrading
production processes
to the extent that health hazards can be
eliminated In the future.
-32-
ucc 031594
1
THIS IS PVC
Manufacturing Polyvinyl Chloride Is produced from Vinyl Chloride by polymerization. Commercial
polymerization processes are classified as follows:
Emulsion Polymerization Suspension Polymerization Mass or Bulk Polymerization.
Emulsion polymerization is the oldest process; here the combination water/
Vinyl Chloride Is transformed into a stable emulsion by the addition of emul
sifiers or soaps (approximately 2%) and under agitation. Polymerization occurs
inside so-called"soap micelles"with the aid of water soluble catalysts such
as Hydrogen Peroxide or Potassium Persulfate. Surfactants such as used today
In detergents,
are added as emulsifiers. The resulting latex
Is converted to finished product by precipitation and spray or rotary
drying.
The suspension polymerization process entails the dispersion of monomer droplets Vthrough )
In water through Intensive mixing ana ^ the addition of suspension stabi
lizers.
Polyvinyl Alcohol and derivatives of
Vact as suspension stabilizers/
celluloselwhicn have the task to further droplet formation and to prevent
sticking of the Individual polymerization particles. The reaction Is initiated
by Vinyl Chloride soluble catalysts. The resulting PVC is separated from the la centrifugue/
water phase by ^ or decanting and dried.
-33-
ucc fr>] SQS
yl
Mass or bulk polymerization of Vinyl Chloride with activators Is accomplished without solvents or dispersants. The main portion of the polymerization proceeds In a powdery state, whereby agitation and heat transfer present special technical problems. From the point of view of processing technology, the mass process shows several advantages over the previously explained processes. Drying of the product Is not necessary. Mass PVC Is also com pletely free of additions such as emulsifiers and protective colloids. Catalyst residues are the only contaminants. The PVC particle is very porous which
favorably affects Its processability.
Properties
\ the j Hardly any other plastic material shows4^ wide range of application possi
bilities of PVC. This Is not only made possible by the various con
version processes but also by the availability of a wide variety of raw Vconstituents;
material ^ and processing aids.
Polyvinyl Chloride's properties are based partially on its chemical composi
tion, Its structural characteristics and the various polymerization techniques,
and partially on the effects of certain additives, which influence the process-
ability and application of the pure raw material. This material is characterized
\suchl Uhe j
by parametersvasiK-Va1ue, particle shape
and particle size distri
bution.
Particle shape,
size and
construction
Influence
Vhave an/
Important product characteristics. TheyHnfluence on bulk density, flowabillty,
and plasticizer absorption and frequently have a bearing on which compounding
i irr -34- 031596
and conversion processes are to be chosen. A particle with good flow characteristics
yfor pneumatic conveying and hopper/
lto processingJ
shows advantages
'V
feeding^ equipment. A
high bulk density has a favorable effect on the throughput In extrusion, operations.
Injection modllng
> /
or mixing The production of dry blends
requires a porous particle construction (with high plasticizer absorption)
In conjunction with good flowablllty of the PVC powder. The viscosity
characteristics of PVC paste formulations are among characteristics which (.Different)
can be Influenced by the polymerization technique.^ Paste PVC's of the same
K-Value, homogenized with the same amount of the same plasticizer could under
the same temperature conditions and residence time lead to completely different
viscosity and flow properties.
Nonplastlclzed compounds show good electrical properties. PYC can be formu late^T^ransparent or opaque compounds.
Nonplastlclzed PVC Is resistant to dilute or concentrated acids and bases,
mineral and plant oils, alcohols and aliphatic hydrocarbons.
*
Rigid PVC formulations show good weathering
properties. If suitable
stabilizers and pigments are chosen. Flexible PVC Is generally less weather
resistant than rigid PVC.
ucc
-35-
031597