The present invention relates to an improved continuous filament mat (CFM) having improved weight variation along the length of the mat and a method of making such a mat.
Continuous Filament Mat (CFM) is a continuous reinforcement fiber, non-woven mat containing a resin compatible binder. CFM is used with polyester, vinyl esters urethanes and other compatible resin systems. It includes continuous fibers randomly oriented in multiple layers with a suitable bonding resin and typically contains a silane coupling agent. CFM is particularly suitable for compression molded electrical and non-electrical laminates, as well as for use in pultrusion processes or any process in which a smooth surface is desired. CFM is used in many fiberglass reinforced plastic (FRP) structural applications such as: compression molding, infusion molding, filament winding, pultrusion, reaction injection molding (RIM), resin transfer molding (RTM), and vacuum bagging. The finished molded products have high equiaxial strengths. Typical products are marine railings, window frames, boat parts, high voltage transformers and corrosion resistant pipes. CFM may also be combined with a woven roving to make a combination mat that has superior processability and structural properties. The reinforcing filaments typically thermoplastic fibers such as glass or polymeric fibers; however, any fiber such as carbon and aramid fibers may be used. For the purposes of the present application, the invention will be described using glass fibers as an example.
Compression molding is a mass production method where molding compounds and other resin glass combinations are compressed in matched metal tools located between platens in a press. Typically, pressures of 150 lbs/in2 and temperatures between 265° F. (130° C.) and 340° F. (170° C.) are used to achieve cycle times of 2-3 minutes. Molding compounds of a thermoset resin, chopped roving, fillers and a catalyst are used in sheet molding compound (SMC). SMC is placed in the tool and covered with a layer of CFM to produce a Class A surface on parts such as automotive body panels, appliance housings and composite doors,
Infusion molding processes such as vacuum assisted resin transfer molding (VARTM) use a single-sided mold that is covered with CFM and other reinforcements and sealed with a flexible vacuum bag or film. A vacuum is drawn on the space between the mold and the seal containing the reinforcements, and a thermoset resin is allowed to infiltrate the reinforcements. The resin flows through the reinforcements and cures to form the finished composite. Large high reinforcement content structural composite parts can be produced to make parts such as boat hulls and windmill blades.
Pultrusion is a continuous process for making lightweight lineal profiles such as reinforcing rods, I-beams and tubing. Pultruded parts incorporate a variety of reinforcements ranging from TYPE 30 single-end roving (available from Owens Corning of Toledo, Ohio), bulky roving, surfacing veils, CFM and woven glass fabrics. After the reinforcement is impregnated with resin, the material is pulled through a heated die that gives it a cross-sectional shape, and is then cured to create the composite profile.
Resin Transfer Molding (RTM) is a liquid molding process where a thermosetting resin is injected into a closed mold cavity to make moderate volume semi-structural or appearance parts. CFM, fabrics, multi-end preform rovings, veils, chopped strand mat and directed fiber preforms can be used in resin transfer molding as reinforcements. In RTM, the dry fiber reinforcement is placed in the bottom half of matching molds, the mold is closed and sealed, and then resin is slowly pumped into the mold. The resin wets through the reinforcement fibers and solidifies to form a composite part such as semi-truck parts and electrical cabinets. The molding pressure is typically lower in RTM than in the compression molding process, therefore, tooling and equipment capital costs are lower than high volume compression molding, but higher than open molding processes.
Vacuum bagging is used to tightly consolidate composites used in windmills, aerospace parts and other applications. Materials that are pre-impregnated with resin are typically laminated with vacuum bagging. The components include a film or fabric, breather medium and plastic film that is applied in sequence on top of a laminate stack in an airtight mold. Air between the mold and film is extracted with a vacuum pump, resulting in a positive-pressure force. This compression forces air and excess resin from the composite laminate or components. Vacuum bagging is also used in conjunction with other processes such as infusion molding and wet lay-up.
CFM is formed by reciprocally depositing continuous reinforcing filaments across the width of a moving conveyor. Typically, a CFM line includes 6-20 fiber draw positions from a source that randomly deposit the fibers across the width of the conveyor. The fiber draw positions may include an idler wheel, a pull wheel and an oscillating finger wheel within the pull wheel. Fibers are drawn from the fiber source, around the idler wheel and over the pull wheel. The oscillating finger wheel penetrates the pull wheel to determine the angle at which the fibers are thrown from the wheel and hence, the position across the width of the conveyor. As the finger wheel oscillates, the fibers are deposited on the conveyor in a saw-tooth pattern having defined period (P). The fibers are thrown from the pull wheel faster than the fibers traverse the width of the conveyor so that the fibers form loops on the conveyor. As shown in EQ. 1, the loop formation ratio (LFR) is proportional to the pull speed (Sp) of the fibers divided by the throw length (L) and the frequency (f). As shown in EQ. 2, the period (P) is proportional to the mat line speed Sml, divided by the frequency (f).
In prior art CFM processes each draw position deposits the fibers independently of the other draw positions in the line.
As the LFR approaches 10, the fibers are deposited in random loops on the collection conveyor. With a decreasing LFR, the loops become less random and the fibers tend to lie transverse to the length of the collection conveyor. At an LFR of 3.25 a distinct transverse array becomes visible and at a LFR of less than about 2.5 the fibers are substantially transverse to the collection conveyor. A high LFR is preferred in CFM because the random loop pattern increases the tensile strength of the mat. A lower LFR provides a mat having a higher tensile strength in the cross-machine direction and a decreased tensile strength in the machine direction.
In the prior art CFM processes, weight distribution in the mat was related to the mat line speed (Sml) and period. Increased mat line speed increased the variation in weight distribution. In order to control the variation, frequency (f) was increased; however, with increased frequency the loop formation ratio decreases and hence the fibers are deposited on the collection conveyor in relatively straight arrays rather than being deposited in loops. In the prior art processes, a period in excess of about 180 mm causes a standard deviation of the weight of the mat in the machine direction to increase above about 2.2, which a variation that is not acceptable for use in a number of composite fabrication processes. Since an increased mat line speed (Sml) increases the oscillation period (P), the maximum line speed is governed by the weight distribution acceptable for use in the composite fabrication process.
The limitations on frequency (f), LFR and mat line speed (Sml) prevent the prior art CFM process from producing mat having a suitable tensile strength at commercially desirable high speeds. New technologies in the composite glass industry, such as gas-oxygen fired furnaces, have increased the melting capacity of furnaces used to produce glass fibers. The increased melting capacity has created a bottleneck in the production line at the CFM line. Additional CFM lines require substantial capital and it is desired to utilize the additional melting capacity while avoiding the capital cost of building new fiber forming and CFM lines.
The present invention provides an improved method of forming continuous filament mat at greater through-put while maintaining or improving product quality by use of a synchronized draw process. The synchronized draw process provides CFM having improved weight variation is capable of operating at increased mat line speed (Sml) and provides CFM having improved structure and tensile strength.
The synchronized draw process may be performed on a standard CFM line with little additional hardware and hence at low cost. The additions to the CFM line include a master PLC 50 that is in communication with forming position 12 via PLC linkage 52. The synchronized draw process may also include a master encoder 54 downstream from the forming position 12 to provide conveyor speed and position data to the master PLC 50 so that the forming position 12 may be individually controlled.
The improved continuous filament mat of the present invention as shown and described herein provides a lower weight variation and is capable of increased and less expensive manufacture by increasing the through-put of a CFM line. The improved product quality and line speed is achieved by use of a synchronized draw process. The synchronized draw process provides CFM having improved filament structure and tensile strength.
The synchronized draw process may be performed on a standard CFM line with little additional hardware and hence at low cost. As shown in
The fibers used in the manufacture of the CFM may be any type of glass fibers, such as A-type glass fibers, C-type glass fibers, E-type glass fibers, S-type glass fibers, ECR-type glass fibers (such as., Advantex® glass fibers commercially available from Owens Corning), or modifications thereof. In addition to glass fibers, any suitable fibers such as, but not limited to, mineral fibers, carbon fibers, basalt fibers, polymer fibers, nylon fibers, polyester fibers, polyamide fibers, aramid fibers, PVC fibers, PVAC fibers, melamine fibers, acrylic fibers, visil fibers, natural fibers, staple fibers, chopped fibers and mixtures thereof may be used.
Glass fibers may be formed by attenuating streams of a molten glass material from a bushing or orifice to form glass fibers. The molten glass may be attenuated rollers which pull the fibers before they are fed to the forming position 12. An aqueous sizing composition may be applied to the fibers after they are drawn from the bushing to protect the fibers from breakage during subsequent processing, to retard interfilament abrasion, and to ensure the integrity of the strands of glass fibers, that is, the interconnection of the glass filaments that form the strand. Sizing compositions are well-known in the art, and typically include a film forming polymeric or resinous component, a coupling agent, and a lubricant. The film forming component of the size composition is desirably selected to be compatible with the matrix resin or resins in which the glass fibers are to be embedded. The sizing composition used in the present invention is not particularly limited, and may be any sizing known to those of ordinary skill in the art or developed hereafter.
The binder composition may optionally contain conventional additives such as dyes, oils, fillers, thermal stabilizers, emulsifiers, anti-foaming agents, anti-oxidants, organosilanes, colorants, UV stabilizers, and/or other conventional additives. Other additives may be added to the binder composition for the improvement of process and product performance. Such additives include coupling agents (for example, silane, aminosilane, and the like), dust suppression agents, lubricants, wetting agents, surfactants, antistatic agents, and/or water repellent agents.
As seen in
The master PLC 50 is typically linked to a Human Machine Interface 50A such as a CRT or video touch screen to provide monitoring, control or override of the master PLC 50.
Prior to formation of a CFM 60, the lay-down pattern from the forming positions 12 are typically calibrated. Calibration determines the mean fiber position of each position 12 and allows for the determination of the profile definition variables. Two potential calibration techniques include forming position calibration and fiber position calibration.
In forming position calibration, the distance between successive forming positions is calibrated and the skew angle of the pull wheel is calibrated so that the position of the fiber strands 32 on the forming conveyor can be calculated. Forming position calibration presupposes careful measurement and calibration between each of the banks of forming positions 12 and between each fiber draw position 12 in the individual banks.
In fiber position calibration, the distance and skew angle of each forming position 12 is not measured but rather the fiber strands 32 are projected onto the forming conveyor and the pull wheel is adjusted, either mechanically or electronically through the master PLC, so that an interval of a known value is achieved. Typically, the interval is set to zero during calibration so that an operator can easily observe the fiber strand 32 position and control the mean fiber position of each fiber draw position 12 so that the mean fiber position from each fiber draw position 12 is overtop the mean fiber position on the first fiber raw position 12 in the bank. The opposed banks are then calibrated each to the other, typically so that they are 180° out of phase.
After calibration, the master PLC 50 is programmed to control the profile definition variables so that a CFM 60 having predetermined properties is produced. Typically, the master PLC 50 linked to the oscillating servo-drive 22 controls the oscillator 20 to drive oscillating finger wheel 18 across a portion of the circumference of fiber pull wheel 14. The position of finger wheel 18 controls the angle at which the fibers 32 leaves the fiber pull wheel 14 and hence the position of the fiber strand 32 on the forming conveyor 10. The master PLC 50 controls the speed and relative positions of finger wheel 18 to control the interval between fiber strands 32. Typically, a the master PLC is preprogrammed with a variety of product specific algorithms for the profile definition variables by controlling the speed of forming conveyor 10, speed of the pull wheel 14, frequency (f), the position of the finger wheels 20 and a time offset between servo-drives 22.
The interval between two forming positions 12 is shown in
It is also possible to control the interval such to form a multi-ply CFM 60 being built up from multiple patterns, such as that shown in
Typically, the fiber draw positions 12 are numbered consecutively down the line, that is, in a twelve position line, position one at the east end of the line while position twelve is at the west end. The positions are typically not centered over the forming conveyor 10 but the even positions (2-4-6-8-10-12) form a bank that is offset to the north side and odd positions (1-3-5-7-9-11) form a bank that is offset to the south side (the ordinal directions are used for the purposes of example only).
In operation, the line operator may select a desired preprogrammed pattern or establish a unique pattern for a desired CFM configuration through Human Machine Interface 50A. Based on the number of on-line forming positions 12, the master PLC 50 then calculate the intervals to lay down the fibers 32 in the desired pattern. The master PLC 50 may then monitor the output of each forming position 12 and, in the event that a forming position 12 goes offline due to a fibers 32 breakout, a mechanical failure or for scheduled maintenance, the master PLC 50 can control the cycle, period, frequency, interval as well as the speed of forming conveyor 10 and the pattern of the forming positions 12 to minimize or eliminate any flaws in the CFM mat 60 and to maintain the product base weight. The algorithms used to control the lay down pattern may include fixed period, fixed frequency or any other suitable algorithm to provide suitable lay down pattern.
In the event that a fiber draw position goes off-line, a PLC 50 using a fixed period algorithm will decrease the frequency (f), reduce the mat line speed (Sml), maintain a fixed oscillation period (P), and increase the interval of the forming position bank to account for the loss of one or more forming position 12.
In the event of a fiber draw position goes off-line, a PLC 50 using a fixed frequency algorithm will decrease the period (P) and the mat line speed (Sml) in order to maintain a fixed frequency and maintain the interval of the forming position bank to account for the decreased period (P) due to the loss of one or more forming positions 12.
By using the inventive method, a synchronized CFM may be formed having reduced weight variation and at increased line speeds. Further, through control of the oscillation rate, it is possible to control the loop formation ratio (LFR) and hence the CM and MD tensile strength of the CFM. Specifically, it is possible to control the CM/MD tensile strength ratio. It is desirable to have a CFM with an increased MD tensile strength in products such as pultrusion. In other products, such as compression molding, infusion molding and resin transfer molding, equiaxial strength may be desired. As shown in
Having generally described this invention, a further understanding can be obtained by reference to certain specific examples illustrated below which are provided for purposes of illustration only and are not intended to be all inclusive or limiting unless otherwise specified.
Table 1 shows theoretically determined properties of four continuous filament mats (examples 1-4). Examples 1 and 2 are based on the CFM technology of the prior art. Examples 3 and 4 are based on the CFM technology of the present invention. As seen in Table 1, Ex. 3 has the same basis weight and mat line speed as Ex. 1, but with significantly lower frequency and peak to valley weight variation and at a higher loop formation ratio (LFR) and period. Similarly, Ex. 4 has the same basis weight and mat line speed as Ex. 2, but with significantly lower frequency and peak to valley weight variation and at a higher loop formation ratio (LFR) and period.
Tables 2A-2C show the data used to create
The data from
The invention of this application has been described above both generically and with regard to specific embodiments. Although the invention has been set forth in what is believed to be the preferred embodiments, a wide variety of alternatives known to those of skill in the art can be selected within the generic disclosure. The invention is not otherwise limited, except for the recitation of the claims set forth below.