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        当前位置:塑胶原料 >> 塑胶百科 >> K-Resin SBC吹膜和流延膜加工指南

        K-Resin SBC吹膜和流延膜加工指南

        文章作者:yiming 发表时间: 浏览次数:



        K-Resin styrene-butadiene copolymers (SBC) are a family of clear resins produced by Chevron Phillips Chemical Company LP. K-Resin SBC were commercialized in the early 1970’s. Since that time, they have grown steadily in the marketplace as more and more applications have been developed utilizing these polymers’ unique blend of sparkling clarity and impact strength. Applications range across the spectra of conventional processing techniques.  K-Resin SBC,alone or in blends with crystal polystyrene, can be extruded into sheet and thermoformed on conventional equipment at high output rates. The favorable economics of K-Resin SBC, along with high productivity, have made possible tough clear disposable drinking cups, lids, and other packaging applications.  These materials process equally well in injection molding, providing good cycle times and design flexibility. An example of an injection molded application is the clear living hinge box. The part is filled through the narrow hinge, yet still has enough toughness to provide good hinge life. In blow molding, K-Resin SBC will process on most conventional equipment, allowing the molder to run a crystal clear bottle without expensive machine modifications, special molds, different screws, or dryers. K-Resin SBC are blow molded in a
        broad range of sizes and shapes, from small pill bottles and medical drainage units, to very tall display bottles. They can also be injection blow molded into extremely high impact bottles with glass-like clarity. Produced as a film, K-Resin SBC makes a clear, stiff, high gloss film suitable for applications such as candy twist wrap, shrink sleeves and overwrap. If extreme processing and regrinding conditions are avoided, the polymers can be reprocessed in multiple passes with minimal change in properties and processing.

        A feature that makes K-Resin SBC more economically attractive when compared to other clear plastics is their low density.  K-Resin SBC have a 20 to 30 percent yield advantage over most non-styrenic, clear resins. 

        All K-Resin SBC grades as shipped by Chevron Phillips Chemical, meet the specifications of the United States FDA Food Packaging Regulation 21 CFR 177.1640 or the specifications of an effective United States FDA Food Contact Notification.  By virtue of this FDA compliance, K-Resin SBC grades may be used as a component of articles for use in contact with food.  Most K-Resin SBC grades meet the food contact requirements for EEC
        Directive 2002/72/EEC and all its amendments.

        Most K-Resin SBC grades have been tested and meet USP Class VI requirements and can be sterilized by ethylene oxide gas, electron beam or gamma radiation. More detailed information on the bio-compatibility of K-Resin SBC can also be obtained in TSM 292 “Medical Applications of K-Resin SBC.”

        K-Resin SBC grades specifically designed for blown film extrusion are K-Resin DK11 and K-Resin  DK13. K-Resin DK11 has high stiffness, excellent clarity, and good permeability. K-Resin  DK13 is not as stiff, has greater elongation and improved tear resistance. Both K-Resin DK11 & K-Resin  DK13 contain a wax, and therefore will require surface treatment (such as corona discharge) before printing.  KRDEV028B is designed for use in the uniaxial oriented film process for shrink sleeves.



        K-Resin SBC film offers exceptional clarity combined with stiffness and excellent gloss. K-Resin SBC can be processed with both uniaxial and biaxial orientation which makes it an excellent candidate for shrink films, candy twist wrap, shrink sleeves and flexible medical packaging. Its low shrink force reduces the likelihood of package deformation and its orientation produces labels
        that shrink uniformly to finished products. K-Resin  film has 100 percent crease retention, making it a preferred choice for candy twist wrap because the twist seal remains in place, keeping the package tightly sealed. K- Resin film can be easily pigmented to make tinted, high gloss transparent or opaque film for decorative films, which may be used as floral wrap or gift wrapping. K- Resin films offer good oxygen, carbon dioxide, and water vapor permeability for produce packaging, which allows fresh cut fruits and vegetables to retain their freshness over longer time periods. 

        K-Resin SBC may be coextruded with barrier or sealant layers for use in many food packaging  applications. As a cast film, K-Resin SBC are suitable for lid-stock applications which demand the ability to heat seal to many different materials. In addition, K-Resin SBC may be processed on extrusion lamination and coating equipment to produce multilayered structures for the replacement of paper and foils.



        K-Resin SBC can be manufactured into both blown and cast films. These two dissimilar processes each offer unique processing merits for K-Resin film production which are worth noting. In blown film extrusion, the film is oriented in both machine and transverse directions, yielding a film with biaxial properties. Cast film extrusion orients the film in the machine direction only, producing a large difference in machine and transverse directional properties. The blown film process is capable of producing either tubes or flat films, depending on the operation of the take off equipment. This makes blown film equipment more versatile in today’s market driven economy.

        Cast film extrusion has advantages as well. The techniques used in the production of wide width films are more easily controlled than in the blown film process. Higher take off speeds are possible, which translates into lower cost per unit weight of film. Cast film extrusion offers better gauge control and gauge consistency, which are critical for thin films below 1 mil (25 microns). Lastly, optical properties such as gloss and haze are typically better when produced on cast film equipment.


        With a few considerations, K-Resin film can be processed on many types of conventional extrusion equipment. Equipment manufacturers offer screw designs specifically for K-Resin SBC.  Extruders may be either air or water cooled, provided they are capable of controlling all barrel zones within 5°F (3°C) of target. Screw cooling is typically not required and in some cases may be detrimental. Extruder feed sections should be equipped with adequate water cooling to prevent polymer bridging at the feed throat. Temperature controllers should indicate set-point and actual temperatures, as well as percentage of heating/cooling. Extruders should be between 20:1 and 24:1 L/D ratios in length. To minimize the residence time of K-Resin SBC in the extruder, extruders having L/D ratios higher than 30:1 should be avoided for blown film  extrusion. For cast film, extruders with up to 32:1 L/D ratios may be used due to the higher output rates, lower back pressures and shorter residence times associated with the process.

        Screw Design

        The design or selection of the extrusion screw is a major consideration in balancing output rate with melt quality. K-Resin SBC are shear sensitive and may be degraded by high shear screws.  A compression ratio of 3.25:1 is recommended for both barrier and single stage screw designs. High shear mixing sections and mixing pins should be avoided for all screw designs. Screw designs which have high compression ratios (above 3.5:1) or special mixing sections should be avoided where possible, but may be used at lower output rates. Gel counts are generally higher when high compression screw designs or special mixing sections are used.Blown Film Equipment

        Blown Film Equipment
        Film Die

        Some conventional bottom fed HDPE or LDPE spiral dies may be used to produce K-Resin blown film with optimum clarity and toughness. Oscillating or stationary dies may be used;although stationary dies are preferred due to their simplicity. In each case, the die should have no stagnant flow areas. Material residence time within the die should be minimized when

        processing K-Resin SBC.  A die opening of 35 – 40 mils (0.9 - 1.0mm) will yield a good
        balance between drawdown ratio and properties for monolayer K-Resin film.  An opening of 40– 60 mils (1.0 - 1.5 mm) is recommended for co-extrusion of K-Resin SBC with olefins.Depending on the die design, larger die openings may result in port lines in the finished film, or limit drawdown capability.

        Air Ring

        K-Resin SBC are amorphous materials, therefore they do not undergo a crystalline freezing transition. K-Resin SBC have relatively high densities, compared to polyolefins, which translate into very efficient heat transfer rates for finished films. These two properties are the reason K-Resin film production requires no special cooling techniques such as internal bubble cooling (IBC) or chilled air at normal processing speeds. The air ring may be a single lip or dual lip design, with certain considerations. Single lip air rings should have short and upright cones and be equipped with a blower capable of controlling the air velocity at very low rates. Air velocity
        control is critical, and consistency of the air temperature and flow rate around the circumference of the air ring is necessary for maintaining a stable K-Resin film bubble.

        Dual lip air rings should have upright cones and be designed such that low air velocity produces a sufficient venturi effect to lock the bubble in the pocket. If the lower air velocity required for K-Resin film processing does not produce a sufficient pressure differential in the air ring, the bubble will not remain stable in the pocket.Dual lip air rings with shallow and open cones are not recommended for K-Resin blown film production due to the shape of the K-Resin® film bubble. However, when co-extruding K-Resin SBC with other polymers, bubble shapes will tend to follow the other material’s processing characteristics.

        Special cooling techniques such as IBC or chilled air are recommended for co-extrusion or very high production rates. Auxiliary bubble stabilization techniques such as bubble baskets or an iris  can enhance bubble stability for both monolayer and coextruded film production.


        Tower and Collapsing Frame

        The tower includes the nip rolls, collapsing frame and any connected bubble stabilizers. Its purpose is to collapse the tubular film bubble into a flattened tube which is free of wrinkles and has the same dimensions as the original bubble. Having the die, air ring, collapsing frame and nip rolls perfectly aligned is critical for producing wrinkle free K-Resin film. The collapsing frame should be designed to contact the bubble a few inches above the frost line.Having the collapsing frame in this position will help keep the bubble
        stable, which will minimize film wrinkles. The tower should be relatively short, or adjustable, to bring the nip rolls fairly close to the die, 12 – 15 feet (3.6 – 4.6 m). Taller towers maybe used, provided that all equipment is well aligned. In this case, a bubble cage is recommended to insure good stability. Film temperature should be maintained as warm as possible to minimize wrinkles, preferably 110 – 130°F (43 – 54°C). K-Resin SBC are fairly stiff materials with excellent crease retention, thus if wrinkles are allowed to form, they will be permanently set into the finished film. 

        The collapsing frame controls the bubble between the top of the die and the nip rolls by using wooden slats, aluminum rollers, or an air frame. Hardwood slats are preferred for monolayer K-Resin film because they impart enough drag to maintain bubble stability, but do not scratch the surface of the film if properly maintained. Aluminum rollers are inexpensive and may be used with many types of materials which offer the processors more flexibility. Air frames improve film cooling and in some cases film surface finish due to the absence of film contact with the collapsing frame. However, for this reason, air frames may cool monolayer K-Resin film too quickly, resulting in wrinkles. EVAs or LLDPEs may stick to wooden slats unless high levels of slip additives are used. In some cases, employing chilled air will reduce drag on the collapsing frame, but may also cool the bubble too quickly, sacrificing bubble stability control or producing wrinkles. Working with a reputable equipment manufacturer to address the specific requirements for the collapsing frame is strongly recommended.

        Nip Rolls

        Perfect symmetry of the nip rolls with the die, collapsing frame and winder is necessary for wrinkle free K-Resin film production. Nip rolls typically consist of one chrome plated and one rubber roll. Oscillating or stationary nip rolls may be used. Temperature control of the rolls is  optional. However, heated rolls may significantly reduce line out time and wrinkles when extruding K-Resin film, while chilled rolls provide improved cooling for polyolefin or coextruded films, which results in increased output rates. The nip rolls must be free of imperfections, including dirt, when processing K-Resin film, as K-Resin SBC will reproduce any scratches, rough patches, or dents in the roll surfaces.

        Film Die

        Cast film dies should employ coat-hanger designs and be equipped with a restrictor bar and adjustable flex-lip die opening. Older cast film dies such as T-dies offer many stagnant areas where polymers can hang-up and degrade, significantly decreasing the quality of the film. A die opening of 35 – 40 mils (0.9 – 1.0 mm) is recommended for cast film extrusion with K-Resin SBC. However, draw resonance may be encountered if the drawdown ratio is too large. If draw resonance is encountered, decreasing the die opening or line speed may improve processing  stability. Draw resonance is discussed further in a later section.
        Air Knife, Edge Pins & Vacuum Box

        To pin the molten web to the chill roll and stabilize the film edges, an air knife may be used to blow a gentle stream of air on the film at the point where it contacts the chill roll. In addition, edge pins may be used to reduce the amount of neck in and also help stabilize the film edges. These techniques are especially useful when producing thin films with large drawdown ratios. A vacuum box may also be used to stabilize the web during extrusion.

        Air Gap

        The air gap is the distance from the die exit to the point where the film contacts the chill roll. This distance can control drawdown ratio and cooling and shrinkage differences in multilayer films. The air gap is typically minimized for K-Resin cast film production. Cast film properties can be altered by adjusting the air gap, however optimization trials are required.

        Chill Rolls

        The chill rolls may be chrome plated and highly polished, matte finished, or embossed rolls. All rolls should be individually temperature controlled by a separate heat exchanger capable of maintaining roll temperatures of 40 – 200°F (4 – 93°C). It is advantageous to use a system which will control the temperature gradient across the entire roll as closely as possible, preferably within 5°F (3°C) maximum variation. The optimum chill roll temperature for K-Resin cast film production will vary with film structure, output rate and equipment. However, 120 – 180°F (49 – 82°C) is typically used for monolayer K-Resin cast film production.



        Corona Treater

        Conventional treating equipment may be used to increase the surface tension of K-Resin films. Corona treatment should produce a minimum of 44 – 48 dynes per centimeter surface energy. For best results, treat and print or laminate the film in line. If it is not possible to convert the film in line, the film should be processed as soon as possible (within 48 hours) after treating.
        K-Resin SBC films, like most films, will lose their surface tension over time. The dissipation rate of the surface tension is dependent on initial treatment levels and storage conditions. If the surface tension of K-Resin SBC film is lower than the level required for printing, the film may be retreated. However, power requirements are generally higher during a second treatment. Therefore, for the same power level of treatment, the surface tension will not be returned to the original level. High storage temperatures will accelerate the loss of surface tension.


        Standard razor blade knives may be used to slit K-Resin SBC films to a desired width. Knives should be kept sharp, and slitting should occur as close to the secondary nip rolls and winder as possible. Care should be taken to protect operators from injuries caused by improper slitter design or operation.


        With good tension control, K-Resin SBC film can be wound successfully on either center or surface winders. Center winders consistently produce higher quality rolls. Regardless of the winder used, it is critical that the winder be properly aligned with the upstream equipment and the film dimensions be maintained without added stress from the primary nip to the slitter. Baggy film or stretched film will hinder wrinkle free roll production.


        Extruder Startup

        It is very important to start the extrusion of K-Resin SBC with clean equipment. This can be accomplished by using polyethylene or commercial purging compounds to purge the system. Introducing K-Resin SBC to the system at operational rates is recommended, provided the K- Resin SBC will follow a polymer with at least a 1.0 melt index or higher flow rate, and the operating temperature is 350 – 400°F (177 – 204°C). If a higher viscosity material is present in the system or operational temperatures are above 400°F (204°C), the material should be purged from the system prior to introducing K-Resin SBC. An operating temperature of 350°F
        (177°C) will minimize K-Resin SBC degradation when it is introduced to the system after purging. Elimination of all contamination using the purge material can take several hours.Fractional melt index purges are recommended for removing K-Resin SBC from the system. Using operational rates will minimize purging time and offer improved cleaning. When using commercial purging compounds, follow the manufacturer’s recommended processing conditions.  The perceived waste of valuable machine time and material during this step is often a motivation for processors to ignore it. More often than not, more material is wasted running
        scrap film than would have been produced during purging. 

        Once the system has been purged, temperatures should be set to 350°F (177°C) prior to extrusion of K-Resin SBC. Residence time of K-Resin SBC at temperatures above 350°F(177°C) should be minimized at all times, particularly during startup and shutdown. Gels, or cross-linked butadiene, will readily form in K-Resin SBC if the material is idle in the extruder,adaptors or die for extended periods of time.

        Chevron Phillips Chemical Company produces a concentrate (SKR 19) which contains a thermal stabilizer, when added at 0.5% or less, will allow K-Resin SBC to be less sensitive to thermal degradation.  Caution should be exercised during startup, as cold spots in the system can produce severe equipment damage if not detected. Always allow the system to soak for at least 30 minutes once the temperature set points are reached. It is not recommended to shutdown the system with K-Resin® SBC in the die or extruder.


        Purging is an integral part of any extrusion operation. Purging should be used to remove polymers from the system before and after material changes to remove degraded or colored polymers and to prepare a system for
        cleaning and shutdown. Fractional melt index LDPE or HDPE resins will readily purge K-Resin SBC from most conventional blown andcast film equipment. Commercial purging compounds will also work well with K-Resin SBC. If an unexpected shutdown or system failure produces degraded K-Resin  SBC, the system should be purged to remove all of the degraded material. Any carbonized material will be very difficult to remove through purging, regardless of its origin, and will ultimately require disassembly of the equipment for complete removal. 

        K-Resin SBC will not purge fractional melt polyethylenes in a reasonable amount of time under most circumstances. To return to K-Resin SBC production, a higher melt index LDPE should be used to remove the purge, followed by K-Resin SBC, preferably at operational rates. Minimizing residence time and operating temperature is recommended when processing K- Resin SBC. Therefore, using K-Resin SBC as a purging material can lead to degradation if output rates are low and temperatures are above 350°F (177°C).



        K-Resin SBC are non-hygroscopic and require no drying under normal storage and processing conditions. However, should K-Resin SBC require drying due to surface moisture caused by high humidity, the material should be dried for one hour at 140 °F (60°C) or 110°F (43°C) for no more than 4 hours. Excessive drying at temperatures above 140°F (60°C) may cause pellet blocking or degradation of K-Resin SBC.

        Anti-block & Slip

        An anti-block must be used with K-Resin film to prevent film blocking. High impact polystyrene (HIPS) can be used as an anti-block (added at ~2 – 3%). Lower levels may not prevent blocking and higher levels will increase the haze level of the finished film. Anti-block is needed when two

        K-Resin film layers come into contact during film production, either on a finished roll, or on the inside of the bubble. If K-Resin SBC are blended with more than 20% GPPS, no anti-block is typically required. A slip additive may be used to reduce the coefficient of friction (COF) of K- Resin® films. Kemamide EZ, an erucamide wax, is the preferred slip additive, and should be used at a level of 0.15%. In general, 0.15% Kemamide EZ in 1.0 mil (25 micron) thick film will lower the COF to 0.2. When using Kemamide EZ, anti-block should be used at a reduced level of 1.5%. This will maintain both clarity and anti-block characteristics. Chevron Phillips Chemical
        makes a slip/anti-block concentrate, SKR17, which can be added at 1-3%. This is specially formulated for K-Resin® SBC and maintains excellent clarity.

        Extruder Shut Down

        To prevent resin degradation, K-Resin SBC should not be allowed to heat soak at even moderate temperatures for extended periods of time. Purging K-Resin SBC from the system at operational rates using a fractional melt index LDPE is recommended. This procedure saves time and material, while ensuring that residence time of K-Resin SBC is minimized. When a shutdown using K-Resin SBC is necessary, reduce operating temperatures to approximately 330°F (166°C) and idle the extruder at a few rpm to allow some movement of material through the extruder and die. This practice will result in less degradation of the K-Resin SBC, while
        minimizing material usage during the temperature change. 


        When reprocessing K-Resin SBC, use a chopper with sharp blades, narrow clearances and adequate ventilation to avoid heat buildup. Chopped K-Resin SBC film may be blended back with virgin resin to reduce material cost. As shown in Table 1, multiple passes of K-Resin SBC through the extrusion process have minimal effect on the film’s properties, providing the regrind is not degraded or contaminated.

        Other packaging films such as EVA, LDPE, LLDPE and HDPE may be blended with K-Resin SBC in the film reclaim stream. The effect on film properties depends on the blend composition and levels, as well as the processing conditions of the finished film. More information is available concerning the blendability of other polymers with K-Resin SBC from Technical Service Memorandum 316 (K-Resin SBC Blends).
         Melt Temperature

         The recommended melt temperature range for K-Resin blown film production is between 360 –400°F (182 – 204°C). To maintain this temperature range, set the extruder, transition, and die temperatures at 350°F (177°C). During startup, record each extruder barrel zone’s temperature and heating/cooling percentage for several hours. If any zone begins to override in temperature, or calls for 75% cooling or more continuously, then the K-Resin® SBC may be subjected to excessive shear in that zone. In some cases, this may be corrected by increasing the temperature setting of the zone. However, the K-Resin SBC melt temperature should be maintained below 425°F (218°C), regardless of individual zone modifications.

        Frost Line

        In the extrusion of K-Resin SBC blown film, the point where the bubble reaches its final diameter marks the frost line position. This is the point where the film temperature falls below the softening temperature of K-Resin SBC. The frost line is not typically visible when processing K-Resin SBC film due to the exceptional clarity of K-ResinSBC film. The frost line should be adjusted to stay between two and four die diameters above the die. For the best bubble stability, the collapsing frame should contact the bubble four to six inches above the frost line. If the frame is not low enough, then a bubble basket, iris, or other bubble stabilizer should be used just above the frost line. 

        Controlling the frost line height is critical to bubble stability and film properties. If the frost line is forced too low, bubble dancing will occur. This will cause wrinkles and gauge inconsistencies. To correct bubble dancing, less air velocity should be used in the air ring. This will reduce cooling, thus allowing the frost line height to move further from the die. Increasing extruder output or decreasing the line speed will have a similar effect. If the frost line height is too high, bubble bouncing, which is a rapid change in frost line position and bubble diameter will occur. This will cause wrinkles and inconsistencies in the film. To correct bubble bouncing, more cooling of the bubble is required. Note the bubble shape diagram, which shows the correct K-Resin SBC film bubble configuration, along with bubble dancing and bubble bouncing.
          The recommended melt temperature range for K-Resin cast film production is between 380 – 420°F (193 – 216°C). To maintain this temperature, set the extruder, transition, and die temperatures to 400°F (204°C). Slightly higher melt temperatures in cast film promote better clarity and drawdown. Due to the reduced back pressures, residence time is typically shorter in cast film than in blown film, allowing for higher extrusion temperatures.

        Frost Line

        The frost line marks the position in the web where the polymer temperature has fallen below the softening point of the material. The frost line should be a straight line across the width of the web, either just before or in contact with the chill roll. Variation in frost line location indicates draw resonance. Variation in frost line shape indicates gauge inconsistencies. In both cases, resetting the die opening and confirming die temperatures are the required initial trouble shooting actions. Note that frost line location may be difficult to determine when extruding K-Resin SBC due to their clarity.

        Draw Resonance

        Draw resonance is a drawing instability that occurs in extensional flow that is between the die and frost line. It is affected by four distinct variables: rheological properties of the material, line take off speed, draw distance, and drawdown ratio. The two most easily adjusted parameters are draw distance and drawdown ratio. In general, if the die gap opening is decreased, a previously unstable web will move closer to or into a stable operating region.  

        K-Resin cast film processing is susceptible to draw resonance if the drawdown ratio becomestoo large. The drawdown ratio for cast film is defined as the ratio of the initial extrudate cross- sectional area to the final extrudate cross-sectional area. Machine directional gauge inconsistency and edge oscillation are products of this phenomenon. The drawdown ratio should be maintained below 60:1 for K-Resin  SBC cast film production.


        K-Resin SBC film is known for its excellent impact, tensile, and optical properties. Variables such as blowup ratio (BUR), drawdown ratio (DDR), additive level, and gauge can have dramatic effects on film properties. More information regarding the effect of BUR, DDR, additive level, and gauge on K-Resin film’s impact strength, tensile strength, permeability, shrinkage, and clarity is available from your regional marketing office.


        K-Resin film has relatively low barrier properties which makes it attractive in several food packaging applications. Packaged fruits and vegetables require a balance of oxygen, carbon dioxide and water vapor to maintain the ripening process and preserve freshness. K-Resin film permeability allows the introduction of oxygen and the release of carbon dioxide and water vapor. K-Resin  film slows the ripening process, however, once the package is opened, normal ripening resumes. This characteristic significantly increases shelf life of the packaged produce. The permeability of K-Resin film may be altered by using additives or by co-extruding K-Resin SBC with other types of polymers. This is very beneficial for applications which need a specific oxygen or carbon dioxide transmission rate. The addition of slip and anti-block additives do not significantly affect gas or water vapor transmission rates when used at recommended levels.

        Blown Film Shrinkage

        Shrinkage of K-Resin film is determined by a modified version of ASTM D2732. The percent of shrinkage in both the machine and transverse direction is directly related to the degree to which the film is oriented in processing. An increase in transverse direction shrinkage is correlated with an increased blowup ratio. An increase in machine direction shrinkage is correlated with increased drawdown ratio. Shrink film made from K-Resin SBC is suitable for packaging goods with a variety of shapes and sizes. The low shrink force property, typical of K-Resin films, allows the film to shrink to the package without deformation of the package. For K-Resin SBC film, the suggested tunnel temperature range is 325 – 350°F (163 – 177°C). For more

        information, refer to Technical Service Memorandum 302 (Shrink Wrapping with Film Made from K-Resin SB Copolymers).


        Corona treatment, at a level of at least 38 – 40 dynes per centimeter, increases the surface tension of K-Resin  film which helps the adhesion of most ink systems. For best results, treat and print or laminate the film in line. If it is not possible to convert the film in line, the film should be processed as soon as possible (within 48 hours) after treating. Inks with a nitro-cellulose base, as well as some water base inks, have been used successfully to print K-Resin  films. For  more information, refer to Technical Service Memorandum 305 (Decorating Methods for K-
        Resin  SB Copolymers).

        Heat Sealability

        To produce bags or enclose products in a package, K-Resin  film may be heat sealed utilizing conventional heat sealing techniques. K-Resin  film typically seals under different processing conditions than most other packaging films. Under proper conditions, heat seal strength will approach film strength. Table 4 lists typical sealing temperature, dwell time, pressure and seal strength for two sealing systems: single and double sealing bar. These seals were formed using a Sencorp ASL/1 laboratory impulse sealer with 0.25 in (6.35 mm) temperature controlled sealing bars. The suggested sealing conditions for K-Resin film are approximately 230 – 350°F (110 – 177°C), 0.3 – 0.5 seconds, and 50 psi (.35 MPa). These conditions will vary with different machines and products. For more information regarding the heat sealing performance of K-Resin  films, contact Chevron Phillips Chemical’s Plastics Technical Center.


         如有疑问可继续浏览更多K-Resin SBC加工指南或联络我公司客户服务中心索取该资料.


        "K-Resin SBC吹膜和流延膜加工指南"由“工程塑料公司”-深圳易欣园塑料化工整理发布,如需转载请注明来源及出处,原文地址:http://www.ineditha.com/baike/K_Resin_SBCChuiMoHeLiuYanMoJiaGongZhiNan/






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