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A Guide to Rotational Figure 1. Various rotomolded toys A Guide to Introduction Rotational molding – also referred to as rotomolding or rotational cast- ing – is one of the fastest growing processing methods today. It’s easy to see why. Rotational molding techniques – coupled with Microthene® polyolefin powders from LyondellBasell – can be used to make hollow items of any size, open or closed, and of any desired shape. In recent years, rotomolding techniques have been developed extensively. On the production line, this process can now compete with or outperform , injection molding and thermoform- ing. In many cases, pieces virtually impossible to fabricate by any other processes can be produced by Figure 2. Smaller storage bins and refuse are also rotomolded rotomolding. Rotational molding was first developed early in the 20th century. Rotomolding is different But it wasn’t until the early 1960s, The main difference between The particles make contact when replaced vinyl LyondellBasell rotational molding and other and melt on the inner surfaces of plastisol resins with polyolefin resins, plastics molding techniques, such the hot molds and fuse in layers that rotomolding gained wide as blow and injection molding, are until all the powder is fused and the acceptance. as follows: desired end product and wall thick- Within a few years, the develop- • resin powder is used instead of ness is obtained. The wall thickness ment of low and high density pellets; is controlled by the amount of specifically designed powder placed in the mold. • the resin melts in the molds for rotomolding enabled rotational instead of being forced under Rotationally molded pieces are molders to enter markets where pressure into the molds in a stress-free except for slight shrink- vinyl parts and processes could not molten state; age forces because the pieces are compete. In the early 1970s, produced without any external pres- crosslinkable and modified polyeth- • the mold has a biaxial rotation; sure. Additionally, there is practically ylene grades made their way into • rotomolding molds are less no scrap in rotational molding. the rotational molding market. expensive because of their These new resins again opened up simplicity; The uniformity of wall thickness more new market areas, especially • and operating pressures are can be maintained to within production of large tanks. relatively low, allowing molds ±10 percent, which is better than that normally possible with the Linear low density polyethylene for to be made from less expensive blow molding process. Wall thick- rotomolding was developed in the materials. nesses can range from 1/32 inch to late 1970s, while the 1980s brought In rotational molding, rigid, resilient 1 inch (0.8mm to 25mm). Most a surge of non-polyethyl-ene resins, hollow bodies are formed by pow- resins used in rotational molding including , and dered plastic material in heated are powders ground to 35 mesh for rotomolding. molds, which are rotated simultane- and ranging in diameter from ously in two planes perpendicular to 74 microns to 2000 microns. each other.

1 Figure 3. Rotomolded products in this photo range from 55-gallon drums to billiard balls 2 Typical rotational molding applications Advantages Rotational molding permits produc- • display window mannequins and of rotational tion of a countless number of fully other hollow display figures of all molding or partially closed items. Design sizes, and; Rotational molding offers signifi- versatility of rotationally molded • playground equipment and cant advantages when compared pieces is almost unlimited. sporting equipment such as golf with other molding techniques or carts, footballs, juggling pins, The rigidity or flexibility of an item : is controlled by the properties of helmets, dumbbells, golf tee • costs for molds and tooling are the resin used (see section on Resin markers, and . relatively low; Choice) and by the wall thickness of Rotomolded parts are also used in • the rotomolding technique is the molding. portable outhouses, battery cases, easily adapted to short produc- light globes, vacuum cleaner and Some typical applications for which tion runs, particularly when sets scrubber housings and garbage rotational molding is particularly of multiple-cavity molds are containers. Furniture, game hous- suited include the following: used; ings, surf boards, traffic barricades, • commercial, industrial and display cases and ducting can also • hollow, totally enclosed items as agricultural storage tanks be produced by rotomolding. The well as pieces with openings can ranging in size from 5 gallons list above indicates just some of the be made; to 22,000 gallons; possibilities. Figures 1-4 illustrate • rotational molding eliminates the • containers for packaging and some of these applications. need for secondary tooling; material handling; • there is little or no waste due to • a variety of industrial parts, Design – almost resin scrap; especially covers and housings, endless potential • wall thickness and piece weight water softening tanks, tote bins; With rotomolding, a plastics can be easily controlled; • numerous under-the-hood and product designer can create a huge • rotational molding procedures in-the-cab automotive parts; array of innovative products. Typical assure uniform wall thickness; • hobby horses, pool tables and design concerns that are handled • deviations can be controlled to many other small or large toys routinely by rotational molding within a maximum tolerance of with complex shapes; include the following: ±10 percent; • baby cribs, balls, dolls, and doll • maintaining uniform wall thick- • pieces with intricate contours parts; ness – rotational molding can and undercuts can be easily provide a more consistently molded; uniform wall thickness for a • virtually any size piece can be part compared to other plastic rotationally molded; processing methods; • there is a minimum of cross- • producing double-wall construc- sectional deformation and tion – rotational molding can warpage; provide uniform double-wall construction on parts; • rotational molding yields pieces with excellent surface detail and • molding thicker corners – due finish; to the process, rotomolded parts will have thicker outer corners • rotationally molded items are which help strengthen the parts; virtually stress free; and • identical or similar items or • molding inserts, reinforcing ribs, different sections on one piece kiss-off ribbing and undercuts – can be molded at the same time these are easily included in a in different colors on a single roto-molded part. spindle; • plastic or metal inserts can often Designers interested in acquiring be molded as integral parts of more specific information can con- the item; and tact the Association of Rotational Molders, 2000 Spring Road, • double wall constructions are feasible. Figure 4. Large storage tanks are Oakbrook IL 60521, (630) 571-0611. a major market for rotomolding 3 The Race Car Bed is rotationally molded from tough, scratch-resist- ant, high impact strength linear low density polyethylene.

Kids are all over this seven-foot- high Big Climber gym rotomolded from weather-resistant polyethyl- ene. The colors have been molded-in, so the parts will not chip, splinter, rust or peel.

This rocking horse comes as either a palomino or a mustang. Both are rotationally molded from polyethylene.

The spinal immobilizer board used by emergency medical services has a rotomolded, linear medium density polyethylene, outer skin and a rigid urethane foam core. 4 Resin choice Melt Index • Type I: Low Density Resins (range of 0.925 g/cm3 and below). To obtain the desired end product, For rotomolding, a resin must have Generally, low density resins are the choice of a quality powdered a good flow when molten. With preferable whenever stiffness is resin is essential in rotational polyethylene, the flow is measured not essential or is undesirable, as molding. One reason is the high by melt index. The higher the melt for many toys, and only when temperatures used risk chemical index, the better the flow. Most light loads are to be expected. rotomolding resins have melt degradation in a less-than-quality • Type II: Medium Density Resins indices ranging from 2g/10 minutes product. (range from 0.926 g/cm3 to to 10g/10 minutes. The term 0.940 g/cm3). Most linear low “g/10 minutes” refers to the weight Table 1. Usage of various resins density polyethylene resins fall for rotational molding of molten resin moving through an within this range. Medium orifice of a predetermined size in density resins are useful for self- RESIN PERCENT OF MARKET 10 minutes. supporting items that require the The melt index is also a rough higher heat-distortion resistance Polyethylene 84% measure of the molecular weight or or stiffness that low density the chain length of a resin. A resin resins do not provide. Polycarbonate with a high melt index has shorter • Type III: High Density Resins Nylon chains and a lower molecular (range from 0.941 g/cm3 to 15% weight or smaller molecules. A resin 0.959 g/cm3). High density with a low melt index has longer resins impart the highest rigidity Polypropylene chains and a higher molecular to the end product, which weight or larger molecules. frequently permits reduction ABS Molecular weight distribution is in wall thickness. Acetals also important in a rotomolding • Type IV: Very High Density Resins Acrylics resin. A narrow distribution is more (0.960 g/cm3 and above.) These Cellulosics advantageous, since the narrower resins are not currently used in the distribution, the more uniform rotomolding. the melt properties. Fluorocarbons 1% In addition to lowering toughness Phenolics Density and increasing stiffness, increasing density raises the melting point, Density is a measure of the specific permits higher temperature limits gravity of a resin. The density of and improves barrier properties in polyethylene is classified by types the end product. according to the American Society of Testing and Materials (ASTM): Today, approximately 84 percent of all resin used in rotational molding is Table 2. How increases in melt index and density of polyethylene polyethylene (Table 1). powders affect processing and end product properties LyondellBasell offers a series of Microthene poly-ethylene powders AN INCREASE IN ...... MELT INDEX . . . . DENSITY with a wide range of properties, AFFECTS THESE PROPERTIES including melt index and density. Melting Point decreases increases While the effects of particle size on end-product properties and Flow increases remains the same processability are less critical, those Impact Strength decreases decreases of melt index and density are considerable. The main effects are Stiffness remains the same increases shown in Table 2. Vicat Softening Temp. decreases increases Resistance to Low Temp. Brittleness decreases decreases Barrier Properties remain the same increase

5 Polyethylene powders – the workhorse of the industry The polyethylene pellets that are small pellet size, can be molded • they are available in a wide range normally produced in the resin without grinding. of densities and melt indices to fit process cannot be the needs of simple, nonstressed have the following used for rotational molding; they items as well as extremely large, characteristics that have made them must be reduced to a much smaller highly stressed applications; the most widely used powders for particle size. This reduction is neces- rotational molding: • they can have their UV stability or sary to obtain good heat transfer outdoor life significantly • they are easily ground to from the mold to the powder. improved by the addition of 35 mesh at high rates; The reduction also improves the pigment or UV stabilizer; • they can be made thermally flow of the particles during melting • they may meet FDA food contact stable with proper stabilization so that oxidation does not inhibit requirements; contact your additives; the moldability and development of LyondellBasell sales or technical the physical properties of the resin. • they can be molded in high- service representative for more The size reduction is usually done temperature, high-speed information; rotational molding equipment by the resin supplier, but can be • they (especially crosslinkable without excessive oxidation; done by the rotational molder who polyethylene) have excellent has grinding equipment. • they have excellent low tempera- chemical resistance making them ture physical properties, such as In addition to mechanically ground ideal for numerous large impact strength, allowing their powder, some resins are available agricultural and industrial use in a broad temperature range; as reactor powder or granules. chemical tanks; Several linear low density polyethyl- • they are relatively low in cost, • they have high dielectric strength enes come in powder or granular making them a material to for use in electrical applications form. Some other resins such as consider in all cost-effective requiring insulation properties, nylon, due to its high melt flow and applications; such as the cherry-picker baskets used by power companies. Table 3. Polyethylene resins: advantages and disadvantages

RESIN ADVANTAGES DISADVANTAGES A new technology that produces “micropellets” can also eliminate LDPE Flexible No stiffness grinding. This technology provides Excellent warp resistance No ESCR small-diameter pellets that, in Consistent shrinkage some applications, mold similarly Most meet FDA requirements 21CFR177.1520 to powder. LLDPE/LMDPE Excellent impact strength Less stiff than HDPE Types of Polyethylene Excellent ESCR Lower heat deflection (See Table 3 for an overview of Good warp resistance temperature polyethylene types) More stiff than LDPE Most meet FDA requirements • Low Density Polyethylene (LDPE) 21CFR177.1520 is flexible and tough, easy to process and has excellent chemi- HDPE Excellent stiffness Low ESCR cal resistance. Good impact strength Warpage and shrinkage Higher heat deflection not consistent • Linear Low Density Polyethylene temperature (LLDPE) or Linear Medium Density Most meet FDA requirements Polyethylene (LMDPE) has better 21CFR177.1520 mechanical properties than LDPE as well as higher stiffness, excel- Crosslinkables Excellent impact strength Longer molding cycle lent low temperature impact Excellent ESCR Does not meet FDA strength and excellent environ- requirements mental stress crack resistance. EVA Copolymers Flexible No stiffness • High Density Polyethylene (HDPE) Excellent cold temperature No ESCR is the stiffest resin of the poly- impact strength Hard to mold ethylene family. HDPE has excel- Consistent shrinkage lent chemical resistance and Most meet FDA requirements 21CFR177.1520 good processability.

6 • Crosslinkable Polyethylene (XLPE) POLYPROPYLENE modification turns conventional contains a crosslinking agent LyondellBasell polypropylene resins polyolefins into Microthene RL that reacts with the resin during are used in applications where adhesive resins that form strong the molding cycle, forming a higher resistance to heat distortion bonds to a variety of substrates, crosslinked molecule similar to a is required for parts requiring such as metals, non-metals includ- thermoset plastic. This reaction autoclaving or sterilization. ing other . improves the stress crack resist- Polypropylene requires cryogenic Microthene RL resins provide resist- ance of the rotomolded part. A grinding to get a powder adequate ance to a wide range of chemicals newer method is called electron- for rotational molding. and are designed for applications beam crosslinking. This process is ONE-STEP FOAM requiring insulation or resistance to a post-molding operation that One-step foam (OSF) is a system corrosion, abrasion or impact. can be done on any type of poly- using several powders and blowing Typical applications include linings, ethylene. Many physical proper- agent pellets to allow rotomolders coating or tie-layers for pipes, ties can be enhanced while the to produce a part with a solid outer drums, tanks or irregularly shaped regulatory status, such as FDA skin and filled with either 2, 4, 7 or parts. Microthene RL resins are approval, can be maintained. 8-lbs/cf of foam. The part, molded normally shipped as powders for The use of post-consumer resin in one step, can range from being application methods such as rota- (PCR) and post-industrial regrind very soft to very rigid. tional lining, co-rotational lining, (PIR) has become an important powder spray and fluidized bed factor in rotomolding because of Rotolining and coating. Since Microthene RL resins increasing concern about solid Co-Rotational Molding bond to metal substrates, surface waste. LyondellBasell has preparation affects adhesion in a performed many studies in this area LyondellBasell Microthene RL resins manner similar to painted systems and can assist you in your are produced by a proprietary and the mold then becomes the application. process that incorporates chemically finished part. reac-tive, functional groups into the New single-site-catalyst technology structure. This chemical allows for the development of new polyethylene grades to meet specific needs. Table 4. Rotational molding resins: advantages and disadvantages Other Rotomolding RESIN ADVANTAGES DISADVANTAGES Resins Polyethylene Low cost Lower impact strength Easy to mold than other resins Some other resins used in roto- molding are: polyvinyl chloride Polypropylene Excellent ESCR Low impact strength at (PVC), nylon, polycarbonate, High heat distortion cold temperatures temperature Higher cost than , polypropylene, flame- Autoclavable polyethylene retardant polyethylene, chemically modified polyethylene, such as Microthene RL Chemical bonding Higher cost than LyondellBasell Microthene resins between resin and other polyethylene material including metal rotolining (RL) resin, and a system called one-step foam, which Polycarbonate Clarity Absorbs moisture incorporates a blowing agent (see Toughness Harder to mold than Table 4). polyethylene POLYOLEFIN Nylon Excellent impact strength Expensive High heat resistance Harder to mold than LyondellBasell has produced a resin polyethylene certi-fied by Underwriters Laboratory (UL) as having a V-0 or non-burning Polyvinyl Chloride Flexible Costs more than rat-ing at 1/8-inch thickness. This Easily painted polyethylene Low stiffness resin allows rotomolders to choose from regular grades of HDPE or Polyester Excellent impact strength Expensive LLDPE rated UL 94 HB or they can in thin-walled applications Harder to mold than use the flame-retardant resin for polyethylene more strin-gent flammability Flame Retardant V-0 rating Lower impact strength requirements. Polyolefin One-Step Foam Foam-filled parts Longer molding cycles

7 Molds for Rotational Molding Inexpensive and Other molds, such as electro- Figure 5. Parting Lines Lightweight formed nickel molds, yield an end product with very fine detail. Vapor- Since very little pressure is exerted formed nickel molds, like electro- in the rotomolding process and formed molds, also yield very good no coring for cooling is necessary, detail but are more costly. CNC- rotational molds can be relatively machined molds and composite simple. Because of this simplicity, molds with jacketed heating ele- the cost of a rotational mold is a ments are also used. fraction of that for a comparable injection or blow mold. Table 5 lists the heat conductivity of metals used for making rotational Two-piece molds are the industry molds. standard, but three-piece molds are sometimes required to facilitate Table 5. Heat conductivity of proper removal of the finished metals used in rotational molds STEPPED parts. Molds can be as simple as a BTU/hr, ft2, g-cal/hr, cm2, round object or complex with °F, in. °C, cm undercuts, ribs and tapers. Steel 26 31 Selection of rotational molds depends on the size, shape and Aluminum 124 148 surface finish of the piece to be Copper 215 257 molded, as well as the number of molds made for a particular piece. Molds should be as thin-walled Flange-Mating and lightweight as possible. Surfaces and Hinges Any of the four types of flange- Types of Molds FABRICATED mating surfaces shown in Figure 5 The most important property of a are suitable. Each mold must be in rotational mold is that its interior two or more sections requiring surface has to be completely non- good parting lines to have proper fit porous. Cast aluminum molds are of the mold sections. Proper fit of by far the most frequently used the parting lines also yields little or molds in the rotomolding industry. no flash of the resin being used and Most parts that are small- to provides correct formation of the medium-sized are molded with finished part. The mating surfaces a cast aluminum mold. should be machined smooth for a Cast aluminum has good heat- good fit and the molds should be transfer characteristics and is cost stress-relieved before the parting effective when several molds of the lines are matched. PIN & BUSHING same shape are required. The only The best parting line cannot drawbacks to cast aluminum are it function properly without a good can be porous and easily damaged. clamping system. The most com- Sheet metal molds are normally mon clamping system for small-to- used for larger parts. They are easy medium parts is the “C” vise clamp to fabricate and, in many cases, the (Figure 6), which can be purchased sections of the mold need only be in any hardware store. Spring- welded together. Sheet metal molds loaded clamps, welded onto the are cost effective when larger sections of the mold, are another single-mold parts are required. popular option. As the molds get larger, nuts and threaded bolts are normally used. The threaded bolts are usually removed and installed TONGUE & GROOVE with an air gun.

8 Figure 6. “C” clamp Venting Molds that have been used with a plastic other than polyethylene Because of the inherent build-up may require special cleaning. Sand of gas in the heating cycle of the blasting with aluminum oxide or rotational molding process, most glass beads is the most effective rotational molds require a venting way. Hand scrubbing with pumice system. and water works, but is very time A vent reduces flash and piece consuming. or mold distortion. It also prevents Environmental concerns have led to blowouts caused by pressure and Mold Mounting the development of water-based permits the use of thinner-walled Molds must be mounted on the mold releases which are taking the molds. spindle or arm of the rotational place of solvent-based releases. molding machine. Large sheet Depending on the size of the mold, Many molders are eliminating mold metal molds are easily mounted by vents can range from 1/8" to 2" releases altogether by having molds bolts or simple clamping systems. inside diameter (I.D.). An industry coated with a fluoropolymer. With cast aluminum molds, a struc- rule of thumb is to use 1/2" I.D. For a complete list of recommended ture commonly known as a spider for each cubic yard of part mold-release agents and conditions can be used to mount several small- volume. of use, contact your LyondellBasell to medium-sized molds on the Since vents leave holes in the sales or technical service same spindle or arm. molded parts, correct placement is representative. The spider consists of several arms essential. The vents should be locat- Figure 7. Schematic of vented or mounting legs to which each ed in an area that may be cut out rotational mold mold is attached, usually by bolts. of the finished part or in an area In turn, the spider has one, central, where a patch does not reduce the mounting location that attaches to aesthetic value of the end product. the machine spindle. This design Figure 7 is a schematic presentation allows two- or three-dozen cast of a vented mold. molds to be mounted on one Vents must also be located to pre- central structure. vent water from entering the part The spider or a single large sheet while it is in the cooling cycle. metal mold may be removed easily Improper venting can cause many with a forklift or crane. This is molding problems, such as water important because the rotomolding tracking on the inside of the end process typically is used for short product. production runs of a variety of parts. MOLD Mold Release Insulation and Since most rotational molds are Coverings designed with little or no draft When openings are desired in rota- angle, it is important to condition tionally molded pieces, insulating the molds with a release agent. lids or inserts can be used. An insu- Normally, molds are cleaned with lating material is applied to an area a solvent and a lightly abrasive cloth of the mold to keep the powder to remove all foreign particles left STAINLESS from fusing at that point. Teflon® on the surface during fabrication STEEL OR TEFLON and silicon foams, among other of the mold. After the mold is TUBE materials, are commonly used. cleaned, a light coating of release agent is applied and baked-on to If thin-walled sections are desired in insure a good coating. With moder- a molded piece, they can also be ate use, the release agent does not obtained by covering a section of adversely affect paint adhesion after the mold with an insulting material flame treatment. GLASS WOOL that results in a small amount of powder sticking to the mold. The wall thickness can be controlled to OIL FILTER CUP a degree by changing the type or thickness of the insulating material.

9 Rotomolding Equipment on a central hub and driven by vari- able motor drives. Most carousels The equipment used in rotational carousel machine (Figure 14). have the freedom to rotate in a molding is relatively simple but has Carousel machines are usually complete circle. many variations (Figure 13). The wheel-shaped. The spindles, each The carousel consists of a heating most common type of rotomolding carrying a a group of molds or a station or oven and a cooling sta- machine is a multiple-spindle or single large mold, are mounted tion. In many cases, the carousel also is equipped with an enclosed Figure 13. Schematic of a system used to obtain mold rotation in two perpendicular planes chamber and a loading and unload- ing station.

MOLD HOLDER The shuttle-type machine (Figure 15) is used most often to rotomold CLAMP larger parts. A frame for holding HINGE PARTING LINE one mold is mounted on a movable bed. Incorporated in the bed are the drive motors for turning the SPIDER UPPER AND LOWER MOLD HALVES mold biaxially. The bed is on a track that allows SECONDARY AXIS SPINDLE the mold and the bed to move into OF ROTATION FIRST DRIVE CONNECTED TO and out of the oven. After the heat- INNER SHAFT ing cycle is complete, the mold is moved into a non-enclosed cooling station. A duplicate bed with a mold is then sent into the oven PRIMARY AXIS OF ROTATION from the opposite end. SECOND DRIVE The (Figure 16) utilizes an CONNECTED TO SPINDLE enclosed oven that also serves as the cooling station. This machine uses only one arm and the heating, cooling and loading/unloading sta- tions are all in the same location. Other types of equipment include “open-flame” and “rock-and-roll.” Figure 14. Carousel type machine The newest type of rotomolding equipment is the Wytkin Composite OVEN Mold Technology (CMT), which utilizes a mold that is electrically heated and air cooled to produce the part (Figure 17).

Heating Stations Most rotomolding ovens are fired by natural gas, using blowers to distribute heat throughout the chamber. Some ovens have the capability to be heated by oil or propane gas, but natural gas is the preferred method. Normal oven temperatures are 400° to 850°F (270° to 454°C). Ovens must be MOLDS well insulated to minimize heat loss. Hot-air convection is the most com- LOAD-UNLOAD STATION monly used heat source, although hot-liquid conduction and infrared COOLING STATION radiation are also used.

10 Mold Cooling Stations Instrumentation levels may cause reductions in the tensile, yield and impact strengths The cooling station may use a Several advancements in instrumen- of the end product. system to provide forced air for tation include computer simulation initial cooling and a water system programs and data monitoring Any appropriate flame or electronic to provide the necessary cooling of systems that help the rotational pre-treatment method can be used the molds and parts. Normally, a molder develop optimum cycle to promote ink and paint adhesion spray mist is used for even cooling. times and improve their molding in and painting. Other than In many cases, however, only air- efficiency. the desired end-product decoration, cooling is used. During the cooling rotational molding requires practi- process, the mold should be Finishing Rotationally cally no post-treatment. If there is rotated. The cooling station may Molded Pieces flash along the mold parting line, it or may not be enclosed. must be removed, although the Pigment loadings in polyethylene creation of flash in rotational mold- powders for rotomolding should be ing is usually negligible. kept to a minimum because high The addition of color to rotationally Figure 15. Shuttle-type machine molded pieces is easily accom- plished. The rotational molder may dry blend a color pigment into the DOOR DOOR natural powder. In this process proper dispersion is essential (one- OVEN STATION 1 STATION 2 quarter of one percent should be the maximum level used). Another way to add color in the MOLD MOLD rotomolding process is by using a resin with compounded-in color. New developments in color technol- ogy allow parts to change color COOLING COOLING LOADING AND UNLOADING LOADING AND UNLOADING when under temperature. Granite and sandstone colors are also available. Figure 16. Clamshell mold Graphics can be molded-in or applied as a post-molding step. ASCENDING UPPER OVEN SECTION Multi-axis routers allow for precision trimming of parts.

Figure 17. CMT technology

MAJOR ROTATION FRAME MOLD MINOR ROTATION FRAME MINOR ROTATION DRIVE

DRIVEMOLD DRIVE

FOLD DOWN MOLD ACCESS DOOR MAJOR ROTATION DRIVE

11 Troubleshooting Guide As simple as it is, rotational molding common problems and their most NOTE: The following guide covers with polyolefin powders is not reliable remedies. If the suggested use of basic polyethylene and, in completely problem-free. However, solutions fail to solve your particular many cases, polypropylene. For most problems encountered can be problem, or if you have other problems with LyondellBasell easily solved with a slight adjust- problems, or if you need assistance specialty resins, such as flame- ment in operating procedures or by in using Microthene polyolefin retardant poly-olefin, one-step choosing a polyolefin powder with powders, contact your foam or rotolining resins, please different properties. LyondellBasell polyethylene sales or contact your LyondellBasell technical service representative and technical service representative. What follows is a Troubleshooting tell them the required end-product Guide – an extensive listing of properties and equipment available.

PROBLEM PROBABLE CAUSES SUGGESTED COURSE OF ACTION Warped parts Inadequate venting 1/2" (13mm) inside diameter (I.D.) vent per cubic yard (cubic meter) of mold volume is suggested for thin- walled parts Non-uniform cooling of the mold caused by Rotate mold during cooling cycle resins pulling away from the mold wall Provide adequate venting and make sure vents are not clogged Use less mold release Avoid large, flat panels in part design if possible Reduce cooling rate during initial part of cooling cycle Increase the cooling medium temperature – air-cool, then water-cool Use all cool air Apply air pressure through spindle during cooling Non-uniform cooling caused by uneven See suggested remedies outlined under the heading part wall thickness Problem: Uneven wall thickness of molded parts Non-uniform cooling caused by shielding Mount mold to eliminate shielding panels Add baffles to direct heat Uneven cooling caused by clogged Check and clean nozzles on a periodic schedule water nozzles Over-cured part. Degradation of the resin due Decrease oven temperature or heating cycle, or to high and/or excessively long heating cycles purge part with inert gas (nitrogen) Highly underfused part. Some degree of Increase oven temperature or total heating cycle underfusion is advisable, especially in the of low melt index resins to prevent Increase heat-transfer rate by using thinner mold degradation.However, highly underfused parts walls, or make the mold from material with greater can cause significant loss in impact strength heat transfer coefficient, e.g., steel, aluminum, copper Improper coloring Select pigment and pigment loading that does not affect strength Use precolored, compounded resin Resin type Use proper resin having adequate melt index and molecular weight distribution for application Moisture on resin or pigment Only use dry powder and/or pigment

12 PROBLEM PROBABLE CAUSES SUGGESTED COURSE OF ACTION Parts stick in mold Insufficient amount of release agent, or Reapply or use more release agent release agent has deteriorated with use Old release agent may have to be removed and new one applied Ineffective mold release, or release agent Use suitable mold release agent that is effective does not withstand elevated temperatures for resin and temperature used; apply according to supplier’s instructions Interference during part removal Locate mold parting line at undercut, or taper sides of mold Roughness and porosity of mold surface Refinish damaged mold surfaces provide areas where resin may adhere (plug weld smooth) Presence of resin at parting line due to Provide adequate venting: 1/2"(13mm) inside internal mold pressures which tend to force diameter (I.D.) vent per cubic yard (cubic meter) of semi-molten resin through the parting line mold volume is suggested for thin-walled parts Build up of degraded resin in the mold may Clean the mold periodically be caused by burning of thin-walled sections Shrinkage onto large deep inserted areas Provide adequate taper Use very effective mold release on insert area Remove part while warm Make adequate provision for applying force to separate mold halves Low shrinkage value for resin Use a higher density resin All of the above Use Teflon coating on mold and/or parting line Poor impact Resin selection not correct Use a lower density or lower melt index resin resistance Density increase during slow cooling Increase the cooling rate to maintain lower density Part design not appropriate Review and alter mold design if necessary, eliminating sharp corners and narrow passages Insufficient fusion of resin Increase temperature or heat time Improper coloring Select pigment and pigment loading that does not affect impact Use precolored compounds Over-cured resin Decrease oven temperature or time Powder bridging or Mold design incorrect Modify mold by increasing width-to-depth ratio not filling narrow across the mold opening passages in mold Design corners or mold with more generous radii. Avoid ribs with width less than four time wall thick- ness Poor pourability (dry flow) of powder Make sure powder has acceptable pourability and bulk density Powder does not melt or flow properly Use a finer mesh powder or a resin with a higher melt index Cold spots on mold Avoid any shielded mold areas Check for mold wall thickness uniformity Add airflow amplifiers Improper mold rotation speed Use correct ratio and location

13 PROBLEM PROBABLE CAUSES SUGGESTED COURSE OF ACTION Long-term part Part under- or over-cured during molding Obtain proper cure failure Photodegradation of part caused by Use a UV-stabilized resin in application ultraviolet light from sun or internal lighting (fluorescent) Add suitable UV stabilizer and/or pigment. A fine, well-dispersed carbon black provides the best protection Stress cracking due to multiaxial stresses in Use stress crack resistant polyethylene grade part; may have been accelerated by chemical environment and temperature Do not store an environmental stress crack solution in a container molded from a poor environmental stress crack grade of polyethylene for a long period of time ar at elevated temperatures Modify design around any area containing inserts Examine part under field conditions to determine adequacy of design and stress concentration points Inadequate resin additive system type and level of inclusion may be insufficient Reduce level of internal mold release if used Color changes due to oxidation Reduce oven residence times Improper colorants or blending Use colorant that disperses well in base resin Compound resin and pigment for a homogenous mixture before grinding Uneven wall Improper mold rotation Vary ratio and speed of the rotating mold to obtain thickness of even coverage and adequate number of powder molded parts trackings Mold shielded Mount mold to eliminate shielding Uneven mold wall thickness Use care in designing molds to prevent excessive variation in mold wall thickness (thin spots attract more resin) Inadequate powder properties. Low bulk Obtain an acceptable powder density, no powder pourability, large amount of fluff, particles have many tails which entangle into clumps during molding Buffeting of air flow in deep dished areas Avoid deep dished areas when possible Reduce thickness of mold in dished areas Open handles so that air can flow through kiss-off in mold Use airflow amplifiers Surface moisture from cryogenic Dry resin before molding grinding (polypropylene only) Too fast fusion (polypropylene only) Lengthen heating time and lower oven temperature Blow holes through Porosity in cast aluminum mold Obtain better quality castings part or ringworm effect under outer Drill through void and drive in pin or weld from part wall surface, outside other than parting line Relieve from outside by drilling into void from side Remove parts from molds while mold is quite warm to touch. This helps drive moisture out of pores Pores or holes in welds Use proper welding rod and procedure. Weld inside surface first to get good penetration

14 PROBLEM PROBABLE CAUSES SUGGESTED COURSE OF ACTION Bubbles on the During the first stages of cooling, there Vent the mold to atmosphere pressure parting line will be a rush of air into the part to fill the resultant partial vacuum. If there is Relocate vent to middle of mold inadequate venting, air will enter molten resin at the parting line and become Use appropriate material in vent trapped as the part wall solidifies Use Teflon vent tube

Vent too small Poor mold parting line Re-mate parting line and adjust mold clamp pressure evenly Clean mold flange to prevent gapping and apply new mold release on flange Excessive flashing at Internal mold pressure during heating cycle Provide adequate venting and make sure vents are mold parting line tends to force semi-molten resin out through not clogged the parting line Re-mate mold parting line and adjust mold clamp pressure evenly Clean mold flange to prevent gaping and apply new mold release on flange Reduce internal most air pressure that is used Use lower melt index resin Long cycles Heat-transfer rate not adequate to melt all Increase heat-transfer rate by using thinner mold the resin, excessively thick mold walls, or make mold from material with greater heat- transfer coefficient, e.g., steel, aluminum, copper Heating not efficient Increase air velocity around mold during heating cycle Low oven temperature Increase oven temperature Recalibrate instruments as they may be reading high Resin powder too coarse Use a finer mesh powder Poor flow Use a higher melt index resin Extended cooling Reduce air-water cooling time ratio Discoloration of Degradation of resin due to high temperature Decrease oven temperature or heating cycle, or inside surface of part and/or excessively long heating cycle purge part with inert gas (nitrogen) Use resin containing the proper amount and type of antioxidant Check pigment for heat stability Uneven heat transfer Mount mold to avoid hot spots Highly underfused Oven temperature not high enough to Increase oven temperature or total heating cycle parts, with many close-up bubbles in the walls of the part small bubbles in wall Heat transfer rate not adequate to melt Increase heat-transfer rate by using thinner mold or rough, powdery all the resin walls, or make mold from material with greater heat- inside surface transfer coefficient, e.g., steel, aluminum, copper Resin powder too coarse Use a finer mesh powder Moisture in mold Reduce moisture in mold by running with warm molds and dry mold before charging with powder Surface moisture from cryogenic Dry resin before molding grinding (polypropylene only)

15 PROBLEM PROBABLE CAUSES SUGGESTED COURSE OF ACTION Speckled color and Insufficient blending Break up agglomerates of pigment before blending lumps of color in Use high intensity mixer. If unable to achieve a dry blended colors desirable color balance, use a colored compound Check for contamination Blow holes through Poor fit on inserts allowing moisture or Refit inserts and relieve to allow trapped gases to part around inserts vapors to be trapped around insert and escape to the outside of the mold expand, blowing a hole in the part Precoat insert with powder Bridging of resin because of close Change insert dimensions or location to allow dimensions powder to flow without bridging Poor part stiffness Part wall too thin Add more powder to the initial charge Resin selection not correct Use resin of higher density Part design not appropriate Review and alter mold design if necessary Underfused parts Increase oven temperature or total heating cycle Increase heat-transfer rate by using thinner mold walls, or make mold from material with greater heat- transfer coefficient, e.g., steel, aluminum, copper Lightning effect Moisture in pigment Dry resin before molding in colored parts Static buildup Apply a small amount of antistat or mineral oil to the resin Pigment not ground properly Use 100 mesh pigment or pulverize pigment Use precompounded colors

Industry associations and information sources The Association of Rotational Molders (ARM), located near Chicago, Illinois, is an international organization representing the rotomolding industry. ARM has compiled an extensive library of literature on rotational molding. It has also published a design manual, the first of its kind for the industry.

Association of Rotational Molders 2000 Spring Road Oakbrook IL 60521 Phone: (630) 571-0611 Fax: (630) 571-0616 E-mail: [email protected] Web site: www.rotomolding.org

Society of Plastics Engineers 14 Fairfield Drive Brookfield CT 06804 Phone: (203) 775-0471 Fax: (203) 775-8490 Web site: www.4spe.org

16 The Rotomolding Process There are six steps in the rotomolding process: The mold or cavity is filled with 1 a predetermined amount of polyethylene powder, such as LyondellBasell Microthene powders. This is called “charging the mold.”

Programming the movement of the arm Weighing the polyolefin powder During the heating/rotation The mold halves are secured 4 cycle the resin melts, fuses 2 together by a series of bolts or and then takes on the shape of clamps. For totally enclosed pieces, the mold being used to form the the entire mold is made of heat- hollow object. conductive metal. When one or When all the powder has fused both ends of the piece are open, 5 into a homogenous layer on the heat-insulating covers are used to walls of the mold cavity, a combi- close the mold. nation of air and water is used in a cooling chamber to cool the mold slowly. This helps maintain the part’s dimensional stability.

Removing the finished item

The molds are removed from 6 the cooling chamber, opened and the finished parts removed. The mold is then readied for the next cycle. Before the molds are recharged and steps one through six repeat- ed, it is important to be sure no Filling the mold moisture is on the inside of the mold. The charged mold is placed in 3 an oven where it is heated and simultaneously rotated around two The mold moves from the oven axes in planes at right angles to to the cooling chamber each other. LyondellBasell Industries P.O. 3646 Houston, TX 77252-3646 United States www.LYB.com

Before using a product sold by a company of the LyondellBasell family of companies, users should make their own independent determination that the product is suitable for the intended use and can be used safely and legally. SELLER MAKES NO WARRANTY; EXPRESS OR IMPLIED (INCLUDING ANY WARRANTY OF MERCHANTABILITY OR FITNESS FOR A PARTICULAR PURPOSE OR ANY WARRANTY) OTHER THAN AS SEPARATELY AGREED TO BY THE PARTIES IN A CONTRACT. LyondellBasell prohibits or restricts the use of its products in certain applications. For further information on restrictions or prohibitions of use, please contact a LyondellBasell representative.

Users should review the applicable Safety Data Sheet before handling the product.

Adflex, Adstif, Adsyl, Akoafloor, Akoalit, Alathon, Alkylate, Amazing Chemistry, Aquamarine, Aquathene, Arcopure, Arctic Plus, Arctic Shield, Avant, Catalloy, Clyrell, CRP, Crystex, Dexflex, Duopac, Duoprime, Explore & Experiment, Filmex, Flexathene, Glacido, Hifax, Hiflex, Histif, Hostacom, Hostalen, Ideal, Integrate, Koattro, LIPP, Lucalen, Luflexen, Lupolen, Lupolex, Luposim, Lupostress, Lupotech, Metocene, Microthene, Moplen, MPDIOL, Nerolex, Nexprene, Petrothene, Plexar, Polymeg, Pristene, Prodflex, Pro-Fax, Punctilious, Purell, SAA100, SAA101, Sequel, Softell, Spherilene, Spheripol, Spherizone, Starflex, Stretchene, Superflex, TBAc , Tebol, T-Hydro, Toppyl, Trans4m, Tufflo, Ultrathene, Vacido and Valtec are trademarks owned or used by the LyondellBasell family of companies.

Adsyl, Akoafloor, Akoalit, Alathon, Aquamarine, Arcopure, Arctic Plus, Arctic Shield, Avant, CRP, Crystex, Dexflex, Duopac, Duoprime, Explore & Experiment, Filmex, Flexathene, Hifax, Hostacom, Hostalen, Ideal, Integrate, Koattro, Lucalen, Lupolen, Metocene, Microthene, Moplen, MPDIOL, Nexprene, Petrothene, Plexar, Polymeg, Pristene, Pro-Fax, Punctilious, Purell, Sequel, Softell, Spheripol, Spherizone, Starflex, Tebol, T-Hydro, Toppyl, Tufflo and Ultrathene are registered in the U.S. Patent and Trademark Office. 5717E/0715

T-Hydro, Toppyl, Tufflo and Ultrathene are registered in the U.S. Patent and Trademark Office.