Document qm60Vd2znEgNm93d2q2nO9oGK
Gen Vinyl Division
Technical Service Bulletin No. 5
Ingredients Used in Rigid PVC Compounding
Although PVC is a very versatile polymer, proper compounding and good lubricant balance are critical in obtaining good machine and end product properties.
Resin
PVC resin is available in a wide range of molecular weights. In the United States, the molecular weight is expressed as inherent viscosity (I.V.); in Europe it is expressed as K value. With both of these values, make sure the value was derived before comparing them. Commercial PVC resins available range from an I.V. of .50 to 1.16 (K value, 47 to 76). The higher the I.V., the higher the molecular weight and the greater the stiffness. Below is a table showing I.V. vs. equipment and end use.
can be formed into a product before it degrades. The stabilizer does this job by absorption of hydrogen chloride, displacement of active chloride atoms, free radical scavenging, disruption of double bond formation, deactivation of degradation byproducts, peroxide decomposition
and ultraviolet energy absorption. Stabilizers in pipe extrusion are
used mainly to process the PVC through the hot hostile environment of the extruder. They do not significantly affect shelf life or weatherability. This is not true in weatherable compounds. In these materials, the amount of stabilizer is five to seven times the level in pipe and they do have a positive affect on weatherability. A given recipe, even
with high levels of titanium dioxide,
I.V. Range 0.50 - 0.65 0.65 - 0.85
0.85-0.98
0.98-1.16
Process Injection molding Injection molding and extrusion Extrusion
Extrusion
End Use
Very complicated molded end use
Pipe fittings - monofilaments sheet, film, profiles, cellular
Pipe, siding, sheet, film profiles, flexible
Complicated profiles (windows), profiles, flexible, wire and cable
Stabilizers
Polyvinyl chloride (PVC) is a heat and light sensitive material. It
degrades by dehydrochlorination and oxidation. This can be seen by the development of color in PVC. In chemical terms, formation of
conjugated double bonds causes the color change. PVC compounds experience heat history in mixing cycles, extrusion/molding, embossing, thermoforming, laminating and scrap rework. Oxidation products occur by exposure to weathering. The job of the stabilizer is to delay heat degradation so that the compound
will have poor weatherability at half the normal level of stabilizer. Any changes in level or supplier of
stabilizers should be checked for weatherability before complete changeover has been made.
There are several types of stabilizers for PVC resin. Below is a partial list:
1. Lead Salts -- These are mainly organic lead compounds like
sulfates, silicates, phosphites, stearates, phthalates and maleates. They are inexpensive and provide good heat stability, excellent electrical properties and
low water absorption. These stabilizers are used in wire, cable
and pipe (in Europe). Potential toxicity and sulfur staining limit their use in pipe in the U.S. Lead stabilizers have some lubricating power and this must be taken into consideration. 2. Calcium-Zinc -- These are used in food contact applications like blow molded PVC bottles, film and sheet. PVC so stabilized can meet FDA requirements. The stabilization power of calciumzinc in PVC is minimal and, therefore, scrap rework capability is poor. They can provide compounds with crystal clarity and low odor properties. 3. Barium-Cadmium -- This type of stabilizer provides good early color, light stability and heat stability. Plate-out tendencies, toxicity of cadmium and poor melt viscosity are characteristic of these stabilizers in PVC. 4. Tin Mercaptides -- These types of stabilizers are the most common ones used to stabilize rigid PVC in the U.S. They give good heat, light and color stability. Another good point is they promote fusion and reduce melt viscosity. The main type of tin mercaptides in use are methyl tins and butyl tins. These are used in pipe, pipe fittings, siding, profiles, cellular vinyl and some bottles. One type of tin mercaptide, di-n-octyltin, is FDA acceptable for food contact applications with PVC. Some of the newer tin mercaptides have external lubrication power and this must be considered in compounding. 5. Stabilizer-Lubricant Package -- (a) Lead Based Systems -- In
Europe, these systems have been used for many years in
pipe. The advantage of this system is that only two or three ingredients must be mixed with the PVC resin instead of
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six to nine The disadvantage is the lack of versatility. (b) Tin Based Systems -- Recently, U.S. tin stabilizer companies have introduced these systems to the U.S. market. They have not penetrated here to the extent of the lead systems in Europe. However, they offer the same advantages and disadvantages as lead systems. We may hear more about them in the future.
Fillers
There are many fillers which can be used with PVC including metal carbonates and silicates, gypsum, clay, alum, barytes and saw dust. The
most common are metal carbonates, mainly calcium carbonate, which is usually in the form of ground limestone and coated with stearic acid. The coating reduces the abrasiveness of the calcium carbonate. It also reduces extruder barrel and screw wear. Calcium carbonate is available in ground and precipitated grades with a range of particle sizes. As a general rule, the finer the calcium carbonate, the better the impact strength of the
finished product. Normally, increasing calcium carbonate content reduces tensile strength and increases tensile modulus. For pressure pipe, the level should never exceed five parts per hundred resin (phr) because higher levels of calcium carbonate could lower the stress design below 2000 psi which is normally required.
Calcium carbonate can be used in PVC compounds to lower the raw material cost of the finished compound. As the level of calcium carbonate increases, the material cost decreases, but the weight per foot of product increases. This is because the specific gravity of calcium carbonate is higher than the specific gravity of PVC. This relationship between compound cost reduction and increased weight per foot must be balanced to give an overall economic reduction. Today, this level is between three to four parts per hundred.
Extruder barrel and screw wear are affected by the amount and the particle size of the calcium carbonate. As amount and coarseness increase, the wear will increase. At levels of five parts per hundred and under, wear is minimal, but higher levels increase
wear drastically. Levels of 25 phr have been reported. This causes barrels and screws to wear out in six weeks. Therefore, this cost must be considered.
Calcium carbonate particles larger than two microns often cause increased barrel wear and reduced
impact strength because they act like holes or stress concentration sites.
Increased levels can also cause a reduction in tensile strength. Other
than as a filler and enhancer of tensile modulus (at high part levels), calcium
carbonate serves no other useful purpose in PVC except to reduce compound cost. It does reduce weatherability of compounds.
Pigments
There are three main reasons to use pigments in PVC compounding: to achieve opacity in non-weatherable compounds, for UV protection in
weatherable compounds and to make a given color. Titanium dioxide is the major pigment used in PVC. Other pigments are used in small amounts to achieve the desired color in combination with the titanium dioxide.
In pipe and some profiles, opacity and color are the main purposes of the pigments. For these uses, titanium dioxide levels are normally between 0.5 phr to 5.0 phr. At these levels, the effect on weathering is minor. Compounds with this level of pigmentation should not be used outdoors. Both color and properties will be drastically affected by long term exposure to UV radiation. The titanium dioxide used in these
compounds is normally controlled chalking rutiles.
In siding, window and other weatherable applications, a high
amount of UV screening is needed. The purpose of this screening is two fold: to maintain color and properties. The major UV screener used in PVC is titanium dioxide. A 15 phr level is needed to achieve this purpose. In colored PVC compounds, a non chalking rutile titanium dioxide is used along with another pigment to achieve the desired color. Because the titanium dioxide has very limited chalking, the color does not fade on weathering to the extent of chalking titanium dioxide. For white compounds, two titanium materials are sometimes used, an anatase and a freely chalking rutile. The combination is used to achieve the right amount of chalking for maintaining the desired whiteness and cleanliness on exposure to UV radiation. This ratio of rutile to anatase is normally 2:1. All changes in weatherable ingredients should be
outdoor weathered two years before being commercialized.
Some normal problems caused by pigments are staining, plate-out, poor dispersion and pinking. Staining is
caused when certain pigments (like lead, cadmium, etc.) react chemically with the atmosphere and the mercaptides of the stabilizer Colored
reaction products are formed. This reaction can occur on processing or on weathering. Therefore, pigments must be carefully chosen in the light of recipe components and the end use.
Pinking is similar in appearance to staining because it forms grey or black streaks on the top three mils of the profile. It seems to come from the action of the compound on the extruder barrel. Changing the melting position in the extruder will often eliminate it. Coated rutile-containing compounds seldom show pinking. However, both anatase and rutile can show pinking. At the present time, we have no clear cut solution to eliminate pinking.
Plate-out is a buildup or deposit on the sizing sleeves, die, embossing roll or screws. Plate-out has often been analyzed to be titanium dioxide and/or calcium stearate, but other materials can cause this problem. The amount of coating on the titanium dioxide can aggravate plate-out, as can exceedingly high stock temperatures. The type and amount of calcium stearate can be another cause. By changing types of lubricant, stabilizer, pigments and processing conditions, the amount of plate-out can be eliminated or controlled.
Processing Aids
The most common processing aids used with PVC are acrylic polymers. Alpha methylstyrene has been used. A process aid reduces melt viscosity, increases frictional heat and reduces uneven die flow. In a compound, it promotes fluxing and acts like an internal lubricant. Increasing levels of processing aid normally allow lower extruder/molding barrel temperatures. Also, it gives the melt hot strength for string-up and drawn-down.
Typical levels are between 0 and 5.0 phr depending on the extrusion process. Single screw high shear and multi-screw extrusion require less processing aid, while low shear, single screw extrusion requires more processing aid. It must be remembered that the type of end product made affects the amount of processing aid used. For example, the more complicated the end product, the higher the level of processing aid used.
Impact Modification
Certain applications require higher impact strength than PVC would
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demonstrate normally. Acrylate, chlorinated polyethylene (CPE),
methacrylate-butadiene-styrene (MBS), and acrylomtrile-butadienestyrene (ABS) polymers are normally used to modify impact strength of
PVC. These polymers provide a shock absorber when the PVC is heated to a high enough melt temperature 196C (385F) to fuse it. At lower melt temperatures, the impact is lower than it would be without impact modification. At this
lower melt temperature, the impact modifier acts like a hole or stress concentrator making the impact lower. Using the proper melt
temperature will ensure that the full properties of the impact modifier will be realized.
All impact modifiers reduce the chemical resistance, tensile strength and stress rupture of PVC compounds. If these properties are desired, the lowest possible level needed to achieve the desired impact should be used. Pipe generally has 0 to 2 phr of impact modifiers, while siding and profiles have 0 to 10 phr. High impact PVC compounds with lower chemical resistance and stress rupture have 6 to 14 phr of impact modifiers. Weatherability can be affected by both type and level of impact modification. Normally, CPE, EVA and acrylate polymers are used in weatherable compounds. They allow good retention of properties, along with good color retention. Both MBS and ABS impact modifiers are poor in
these characteristics, but are good for low temperature properties.
Impact modifiers generally promote flux, with the exception of CPE. As flux promoters, they tend to reduce the temperature of the extruder barrel needed for a given melt temperature. This point needs to be considered when compounding PVC.
Lubricants
Lubricants are materials that control the fluxing (melting) point in the
extruder/molder to achieve the best processing characteristics and physical properties. There are three types of lubricants. They are external, internal, and external/internal. They
are defined by their effect on the melt in a plasticizing screw, as follows'
External Lubricants -- Provide good release from metal surfaces and lubricate between the individual PVC particles. As the level of external lubricant is increased, it moves the melting point of the PVC in the direction of the die.
Internal Lubricants -- Provide lubrication at the molecular level and reduce the melt viscosity. The internal lubricant moves the melting point of the PVC in the direction of the extruder hopper as it is
increased in level. External/Internal Lubricants --
These materials provide both external and internal lubrication depending on the combination of chemical groups contained.
External Lubricants
External lubricants are normally non-polar molecules or alkanes. They are usually paraffin waxes, mineral oils or polyethylene. Some stabilizers have oils that carry active ingredients such as external lubricants. External lubricants are normally incompatible with PVC. They help the PVC slip over the hot melt surfaces of the dies, barrels and screws without sticking and contribute to the gloss on the end product surface. Extruder motor amperage is greatly affected by small changes of external lubricants.
Common problems resulting from over-lubrication include: surging of the extruder, lumpiness of the extrudate, incomplete fusing and the necessity of high barrel temperature. In the end product, low impact strength and acetone failure are the common manifestations found.
Internal Lubricants
Internal lubricants are normally polar molecules. They are normally fatty acids, fatty acid esters or metal esters of fatty acids and are very compatible with PVC. They lower melt viscosity, reduce internal friction and promote fusion. Common problems of under lubrication are rough extrudate, adhesion to metal surfaces, melt fracture, quick fusion and abnormally low barrel temperatures. In the end product, burning, plate-out, matte
surfaces and poor impact strength are typical results of underlubncation
External/Internal Lubricants
These are hard to define because they have chemical groups (polar and non-polar) of both lubricant types. In
general, they have long hydrocarbon chains, along with amide, alcohol, acids and ester groups. Common types used in PVC are fatty acid amides and oxidized polyethylenes Some of these materials will lubricate as an external lubricant before melting and as internal lubricants after melting. Others will do the reverse. Each of these lubricants should be characterized for its type of lubrication in a given compound.
The purpose is to achieve the full properties of PVC and a melt that will extrude or mold without problems, at an economical cost. To achieve these goals, experiments must be performed. A bench extruder can be used for gross compounding. But, the final compound will need to be run on commercial size equipment. This is the only proof of the "goodness" of the compound. Avoid over-compounding for
machine problems. After a compound has been developed, tested, and used successfully, usually very little change is necessary. Before any recipe changes are made, equipment should be thoroughly checked.
Temperature controllers and thermocouples should be connected properly and the reading checked. Screw rpm, back pressure instruments and heat bands should be checked. All operating procedures should be compared with previous successful runs with the same compound. Cleanliness and freedom from obstruction of screen packs, nozzles, adaptors and dies should also be checked. If all are correct, establish clearly what is wrong with
the melt before changing the recipe. An attempt should be made to correct a specific problem in the melt rather than a symptom in the end product which could have many causes. After all of these points have been checked and the problem is still present, the recipe should be changed.
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UlFGoodrich
Geon Vinyl Division
6100 Oak Tree Boulevard Cleveland, Ohio 44131 216-447-1131 1-800-GET-GEON (1-800-438-4366)
Domestic
Sales Offices
GREAT LAKES MIDDLEBURG HTS., OH 44130 7550 Lucerne Drive, Suite 115 216-234-1330 1-800-GET-GEON (1-800-438-4366)
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International
Sales Offices
The BFGoodrich Company Geon Vinyl Division International Sales 6100 Oak Tree Boulevard Cleveland, Ohio 44131 USA Cable Address GOODRICHCHEM Telex: 980427 GOODCHEM IDPC Telex: 423313 BFGCLZINT
WATERLOO, ONTARIO, CANADA BFGoodrich Canada 195 Columbia Street West N2J4N9 519-888-4300
HONG KONG BFGoodrich Chemical (Far East) Ltd Suite 1406, AIA Building No. 1 Stubbs Road 5-743224 Telex' 780-83061
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BFGOODRICH CHEMICAL - EUROPE Excelsiorlaan 40-42, B.6 1930 Zaventem, Belgium Telex. 846-20921 Phone: 32-2-725-2233 Telefax: 32-2-725-2352
BFGoodrich The BFGoodrich Company, Geon Vinyl Division/6100 Oak Tree Blvd . Cleveland, Ohio 44131
iFGoodrich
The information contained herein is believed to be re* liable, but no representations, guarantees or warranties of any kind are made as to its accuracy, suitability for particular applications or the results to be obtained therefrom The information is based on laboratory work with small-scale equipment and does not necessarily indicate end product performance. Because of the variations m methods, con
ditions and equipment used commercially in processing these materials, no warranties or guarantees are made as to the suitability of the products for the application dis closed Full-scale testing and end product performance are the responsibility of the user BFGoodrich shall not be liable for and the customer assumes all risk and liability of any use or handling of any material beyond BFGoodnch's
direct control The SELLER MAKES NO WARRANTIES. EXPRESS OR IMPLIED. INCLUDING. BUT NOT LIMITED TO. THE IMPLIED WARRANTIES OF MERCHANTABILITY
ANO FITNESS FOR A PARTICULAR PURPOSE Nothing contained herein is to be considered as permission, rec ommendation, nor as an inducement to practice any pat ented invention without permission of the patent owner
Printed in U.S A.
February, 1990
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