Mold for manufacturing a fiber reinforced polymer utility vault lid
11613052 · 2023-03-28
Assignee
Inventors
- Edward J. Burke (Temecula, CA, US)
- Thomas Atkins (Newport Beach, CA, US)
- Brian Anthony Beach (Rancho Cucamonga, CA, US)
- Robert Gwillim (Temecula, CA, US)
- John A. Neate (Niles, MI, US)
- Richard Clark Powell (Murrieta, CA, US)
Cpc classification
B32B2262/00
PERFORMING OPERATIONS; TRANSPORTING
B29C69/00
PERFORMING OPERATIONS; TRANSPORTING
B29C43/02
PERFORMING OPERATIONS; TRANSPORTING
B29K2067/00
PERFORMING OPERATIONS; TRANSPORTING
B29C33/10
PERFORMING OPERATIONS; TRANSPORTING
B32B27/06
PERFORMING OPERATIONS; TRANSPORTING
B32B27/00
PERFORMING OPERATIONS; TRANSPORTING
B32B2435/00
PERFORMING OPERATIONS; TRANSPORTING
B29L2031/10
PERFORMING OPERATIONS; TRANSPORTING
B29C43/22
PERFORMING OPERATIONS; TRANSPORTING
B32B37/24
PERFORMING OPERATIONS; TRANSPORTING
B32B2367/00
PERFORMING OPERATIONS; TRANSPORTING
B29K2105/12
PERFORMING OPERATIONS; TRANSPORTING
International classification
B29C43/02
PERFORMING OPERATIONS; TRANSPORTING
B29C33/10
PERFORMING OPERATIONS; TRANSPORTING
B29C69/00
PERFORMING OPERATIONS; TRANSPORTING
B32B27/00
PERFORMING OPERATIONS; TRANSPORTING
B32B27/06
PERFORMING OPERATIONS; TRANSPORTING
B32B37/24
PERFORMING OPERATIONS; TRANSPORTING
B32B38/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method of manufacturing a fiber reinforced composite material lid for an utility vault including mixing an unsaturated polyester thermosetting matrix in to a resin paste, compounding the resin paste into a fiber reinforced composite material, maturing the compounded fiber reinforced composite material, cutting the matured compound into a charge pattern, molding the charge pattern in a mold cavity of a heated mold under low pressure to form the lid and cooling and machining the lid. The mold includes a cavity die and a core die having a shear angle for interfacing the core die within the cavity die and a steam pot for heating the cavity die and the core die, wherein the lid is molded between the cavity die and the core die and removed from the mold by a lid ejection mechanism.
Claims
1. A mold for molding a fiber reinforced polymer material utility vault lid comprising: a cavity die having a mold surface; a core die having a telescoping shear edge for interfacing the core die within the cavity die, wherein the fiber reinforced polymer material utility vault lid having a plurality of individual fibers within polymer material is molded between the cavity die and the core die; and a lid ejection mechanism for removing the molded lid from the mold; wherein the mold surface of the cavity die has a textured surface along the entire mold surface comprising a pattern of non-uniform spaced recesses extending into the mold surface of different sizes and depths and a plurality of protrusions of irregular height, size and shape, a protrusion of the plurality of protrusions being positioned between each recess and extends outwardly to engage and push the individual fibers of the fiber reinforced polymer material utility vault lid inwardly away from an upper surface of the lid to create a resin rich layer above the individual fibers along the upper surface of the lid during molding and preventing the individual fibers from reaching the upper surface of the lid.
2. The mold of claim 1 further comprising means for aligning the cavity die and the core die.
3. The mold of claim 2 wherein the means for aligning are alignment pins and bushings.
4. The mold of claim 1 wherein the telescoped shear edge provides for a gap between the core die and the cavity die to allow air to escape during a molding period.
5. The mold of claim 1 further comprising means to heat and control temperature of the cavity die and the core die.
6. The mold of claim 5 wherein the means to heat and control temperature is a steam pot including internal supports and a sealing plate.
7. The mold of claim 1 wherein the lid ejection mechanism are pins extending through the die core and actuated by a pin plate.
8. The mold of claim 7 wherein the pin plate is hydraulically actuated.
9. The mold of claim 1 where the cavity die further has a plurality of boss recesses for forming bosses on an upper surface of the lid.
10. The mold of claim 9 wherein the boss recesses are of varying depths.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
(4)
(5)
(6)
(7)
(8)
(9)
(10)
(11)
(12)
(13)
(14)
(15)
(16)
(17)
(18)
(19)
DETAILED DESCRIPTION
(20) Referring to
(21) Referring to
(22) Before the fiberglass reinforced polymer matrix sheet can be used for molding it must mature. This maturing time is necessary to allow the relatively low viscosity resin to chemically thicken. The sheet is kept in a temperature room until the desired molding viscosity is reached. When the sheet is ready for molding it is cut into pieces of a predetermined size. As shown in
(23) The mold is heated, for example, by steam. After the charge is placed in the mold cavity, the mold is closed and the charge is compressed. The fiber reinforced polymer matrix material is a flowable compound and under heat and pressure is transformed from a thick paste to a very low and optimized viscosity liquid of viscoelastic state. The material flows to fill the mold cavity. As seen in
(24) Referring again to
(25) Referring to
(26) The top, bottom and sides of the mold assembly can be insulated to contain the heat required for the process. It also insulates the heat from the machine or hydraulic press to manufacture the part.
(27) Example Manufacturing Process for an Embodiment of the Invention
(28) TABLE-US-00001 Mixing and Storing Polymer Formulation Ingredients Desired % Range Polyester Resin 23.25 10-40% Polystyrene (Shrink Control) 11.46 5-30% Catalyst 0.39 0.1-8% Inhibitor (PBQ) 0.26 0.1-8% Fiber Wetting Additive 0.35 0.1-8% Zinc Stearate (Mold Release) 1.21 0.1-8% Inorganic Filler 24.99 15-50% Magnesium Oxide (Thickener) 1.21 0.1-8% UV Stable Pigment (Gray) 1.89 0.1-10% Fiberglass (0.5″-2″ Chopped) 35.0 5-60%
(29) The polymer formulation is typed into an automated delivery system. This system is responsible for mixing of all of the ingredients together, storing the polymer matrix and then delivering it to a compounder, for example a Schmidt and Heinzmann (S&H) Compounder.
(30) The formulation is mixed to ensure that the material is homogeneous. Controllers manipulate the order of addition, dwell time, blade speed and mixing temperature. Upon completion of paste matrix mixing cycle, several tests are performed to make certain the paste is correct before being released to a holding tank. The holding tank's primary function is storage. During the storing process, the paste matrix is agitated by low shear mixing blades. If the weather is less than 65 F degrees a water blanket is used to make sure that the paste does not lose temperature. This loss can influence the thickening response and negatively impact the moldability of the material. The holding tank is placed on a scale and is continuously metered gravimetrically to the compounder during manufacturing. The polymer matrix still does not have color or the thickener (polymer extender). Both of these ingredients are added separately to ensure that there is not any cross contamination in color or troublesome thickening because of improper maintenance. The “b-stage” component is tested to confirm the desired formulation before it is released into production.
(31) Batch mixing is typically used when formulation flexibility is required. When the lids are manufactured with one formulation, a continuous process can be employed. This allows the mixing process to be tailored to one specific formulation. All of the ingredients are continuously fed to a mixer, typically an extruder. They are blended together in the extruder and introduced into the compounder. This process eliminates the additional equipment needed to feed and mix the b-side.
(32) Matrix and B-Stage Delivery
(33) The automated delivery system will determine pump rates needed for manufacturing. This system will determine the amount of paste delivered per hour to the compounder based on the matrix specific gravity, product weight, glass percent and sheet weight. The matrix and b-side are combined by running through a series of high shear cowls type mixing blades or a static mixer. The mixed material is then stored in a surge tank and delivered to the compounder with stater pumps. Inside of the doctor blades on the compounder are height sensors. The height of the material in the doctor boxes is controlled by the automated delivery system.
(34) Compounding
(35) There are many variable that can be changed on the compounding machine such as:
(36) TABLE-US-00002 TABLE 1 Preferred Values Range MACHINE Belt Speed 5 m/min 3-20 m/min Cutter Speed 167 RPM 100-668 rpm Feed Roller 2.5 Bars 1-5 bar Rubberroll 3.5 Bars 1-5 bar Oscillation 2.0 Bars 1-5 bar Winding Counter 250 100-300 rpm Holding Tank Temperature 95 F. ± 5F. 60-120 F. Final Mixer Tank Temperature 95 F. ± 5F. 60-120 F. DOCTOR BOXES Lower Dam Height 0.069″ 0.050″-0.120″ Upper Dam Height 0.069″ 0.050″-0.120″ Dam Sides Height 0.065″ 0.020″-0.100″ Level SP #1 38 mm 20-80 mm Level SP #2 38 mm 20-80 mm POLY FILM Upper Film Tension 6.0 Bars 2-10 bar Lower Film Tension 6.0 Bars 2-10 bar Sheet Width 34½″ 10″-80″ Deflector Width 35⅛″ 8″-82″ COMPACTION UNIT Belt Tension (Upper) 4 Bars 2-10 bar Belt Tension (Lower) 4 Bars 2-10 bar Impregnation Bridge Lower Range 9.5 Bars 4-12 bar Turret Winder 4 Bars 2-8 bar Smoothing Roller Up/Down UP up/down
(37) Since the specific gravity of the material is known, the height of the doctor blades can be determined based on the product weight of the material. The product weight of the compound is measured by the weight per unit area. Typically weight is measured in grams/ft.sup.2. The fiberglass component can also be measured. Varying the RPMs of the chopper will linearly change with the weight of the fiberglass. The product weight of compound is 545 g/ft..sup.2.
(38) Paste samples (matrix and b-side together) are taken throughout the run and measured with a viscosmeter. Typical measurements are taken initially, at 24 hours and at 36-60 hours. Several variables are considered when determining the thickening curve: temperature, initial viscosity and molding viscosity. These values are optimized based off of prior compounding and material trials. When lot number of either the resin or the thickener change, a thickening study is run to determine if the levels need to be changed. The target molding viscosity of the material is between 20-45 MM cps. Viscosity measurements are taken with a Brookfield DV-II.
(39) After the polymer matrix is introduced to the fiberglass the sheet is then squeezed together between serpentine rollers to wet-out the fiberglass. Since this process yields structural parts, a ft.sup.2 template is used to cut a sample of the material. If it falls within a predetermined range, the material is qualified for release.
(40) The product weight samples are collected and used to mold lab panels. During the molding a sensor detects the dielectric properties of the material and determines the gel and cure time of the material. The cured panels are then cut up into various samples for testing. Typical testing includes tensile strength, flexural strength, specific gravity, fiberglass content and water absorption.
(41) TABLE-US-00003 TABLE 2 Physical properties measured on 0.120″ thick panel molded 24 Hrs. after manufacture. Molding Conditions: 3 min. at 330° F. Molding Pressure = 200 psi. Coverage = 60% Property (units) Desired Range Gel Time (s) 35-50 Cure Time (s) 87-105 Product Weight (g/ft.sup.2) 534-556 Specific Gravity (g .Math. cm.sup.−3) 1.63-1.67 D3 to D5 Viscosity (Cps) 23-35 Tensile Strength (psi) 15,700-18,300 Flexural Strength (psi) 26,000-31,500
(42) Once the material has reached the predetermined values of the quality testing, the material is released into production.
(43) Molding Process
(44) FRPM The fiber reinforced polymer matrix (FRPM) Compound is delivered to a self aligning actuating mold (SAAM) area on roller carts that hold (8) rolls of compound weighing approximately 200-500 lbs. each, or in a box with 500-6000 lbs. Each roll has a tag that identifies Manufacture Date, Formulation, Batch #, Roll# and Weight. Material is not released until it has passed all QC requirements as detailed in the Compounding section. The carts are staged at the FRPM Cutting area where the automated slitter is located. The SAAM Production Molding Operation Notebook is referenced which shows the charge size and weight for the particular lid that is to be molded. Once the sheet is located the correct cut sheet and the slitter is set to automatically cut the charge to size and de-film the compound. The cut charge sheets are then weighed to the correct charge weight and stacked in completed individual charge packs ready to manufacture.
(45) SAAM Press A SAAM system enables large platen area presses to be designed & installed without the need of installation pits. Other press types are also applicable. The use of a self aligning press was accomplished by inverting the hydraulic cylinders that supply the pressing tonnage. The use of a self aligning press also allows for any change in location of the press, to meet any change in production demands, to be carried out with a minimum of disruption to the production facility. To support the SAAM production molding system a special Low Pressure Molding Compound (LPMC) was developed and FRPM (Fiber Reinforced Polymer Material) is a form of LPMC. The Platen SAAM system allows for the interchange of steel tools (molds) in the normal way. The tools at present are as follows: 15″ round (1400) 13″×24″ lid mold (1324) 17″×30″ lid mold (1730) 24″×36″ lid mold (2436) 24″×48″ lid mold (2448) Split 30″×48″ lid mold (3048) Typical SAAM Operating Pressures: 3,000 psi Cylinder bore: 12 inch Rod diameter: 5.5 inch Effective area of cylinder: 89.34 square inches At 3,000 psi hydraulic pressure the cylinder develops 268,017 lbs. of force Therefore, four (4) cylinders develop 1,072,068 total lbs./536 tons of force A 17″×30″ lid has a plan view surface area of 17″×30″: 510 square inches 1,072,068 lbs. of force divided by 510 square inches equals 2,102 psi molding pressure A 24″×36″ lid has a plan view surface area of 24″×36″: 864 square inches 1,072,068 lbs. of force divided by 864 square inches equals 1,241 psi molding pressure A 24″×30″ lid has a plan view surface area of 24″×30″: 720 square inches 1,072,068 lbs. of force divided by 720 square inches equals 1,489 psi molding pressure. The molding pressures get halved when molding two-up in the same SAAM. The plan view surface area is smaller than the total surface area so when using the plan view area around 400 psi molding pressure is utilized.
(46) Molding Procedures The press is preheated to ensure the proper settings. A notebook of Master Control Settings is consulted for the sheet for the particular lid to be molded and screens 1 and 2 are set to the proper Control Settings. This Master Control Settings Record Sheet shows proper setting for each of the following:
(47) TABLE-US-00004 Value Range SCREEN 1 1. Open Position 52″ 42″-60″ 2. Load Position 42″ 35″-52″ 3. Slow Down Position 34″ 33″-35″ 4. Closed Position 31.5″ 32″-25″ 5. Cure Time 400 sec. 150-600 sec. 6. Fast Speed 0.8 IPS 0.1-1.0 IPS 7. Slow Speed 0.2 IPS 0.1-1.0 IPS SCREEN 2 1. Top Poppet Auto Time 50 sec. 0-100 sec. 2. Bottom Poppet Auto Time 50 sec. 0-100 sec. 3. Top Poppet Manual Time 10 sec. 0-100 sec. 4. Bottom Poppet Manual Time 15 sec. 0-100 sec. 5. Ejection Time 25 sec. 0-100 sec. 6. Maximum Slow Cure Time 99 sec. 0-100 sec. The operator reviews the temperature indicators on the master Control panel to see if the molds are up to the proper temperatures, 325° F.-270° F. for upper tools and 320° F.-265° F. for lower tools. Once the screens are checked the operator take a hand held temperature gauge and verifies that the mold temperatures match the screen readings from the thermocouples. He is also verifying that the upper mold is always hotter than the lower mold to avert any telescoping shear edge mold crash. Once the temperatures are verified the operator then visually inspects the mold surfaces for cleanliness and any sign of debris or scumming. If any is seen it is removed with brass tools and air streams. The press is then set into Automatic mode and readied for the molding of the first part.
(48) Molding Operation The delivered charges are inspected and measured to ensure they are the correct size and weight. The first charge is staged on the scale and the weight is noted. On the PROCESS DATA &PARAMETERS MASTER CONTROL SETTINGS RECORD SHEET there is a heading “CHARGE DIMENSIONS”. Under this headings are the following line items that contain the proper information regarding the charge for example, a 17×30 (1730) charge:
(49) TABLE-US-00005 Value Range 1. Weight LBS.: 26.1 lb 26.1-26.6 lbs 2. DIMENSIONS: 28.5″ × 16″ 16″-30″ × 8″-17″ 3. NUMBER OF LAYERS: 8 5-15 Once the charge has been confirmed to meet specification, the green “CYCLE START” button is pushed to activate the automatic molding cycle and the mold lowers to LOAD POSITION. Once the mold stops to the load position, the charge is delivered into the mold via a loading device and the charge is precisely position on the lower mold being centered in each direction. As soon as the loading tool has exited the mold parameters, the operator again pushes the green “CYCLE START” button and the press lowers from “SLOW DOWN POSITION” to “CLOSED POSITION”. Once the presses sensors confirm that each corner is at Full Closed position, the “CURE TIME” cycle starts. As the automated cycle starts the operator inspects and places the next charge onto the scale again verifying the weight. After the CURE TIME cycle is completed, the air poppet is automatically activated and the press opens to SLOW SPEED position and then opens to FAST SPEED and returns to the OPEN POSITION setting of the cycle. As the press is opening to OPEN POSITION and the mold has cleared the full extension dimension of the ejector pins and reaches a preset clearance height, the ejector system is activated and the part is raised above the lower mold surface to the full height of the ejection pins. As soon as the ejectors have reached full height, the Unload Tool is inserted under the part and the ejector rods are automatically lowered. Once the ejectors are back in full rest position, the Unload Tools is extended to the front of the press and the part is delivered to the operator to do a visual inspection, deflash the edges and place in the cooling cart. Once the part and the Unloading Tool have been removed from the press parameters, the operator visually inspects the mold surfaces and clears and debris with an air stream. The cycle begins all over repeating each of the documented steps.
(50) Machining Each Cooling Cart handles multiple parts. As the carts are filled they are removed from the SAAM area and placed in a staging area to cool and stabilize. During this period the parts are randomly inspected by QC and verified to meet quality specifications dimensionally, weight and appearance. The parts need to cool to less than 150° F. prior to any machining being done to the part. This cooling process ensures the dimensional stability and flatness of the part prior to machining. The machining operator will go through the start-up checklist contained in the computer numerical controlled (CNC) Operations manual and once the checklist is complete he will set the machine to the appropriate machining program corresponding to the sized lids being machining. The CNC has been programmed to machine one part at a time. Each lid has its own program. The operator removes a part from a cooling cart and places it in the designated position for the machining cycle. Once the part is positioned the operator will activate the vacuum holding the part in proper position. The Operator pushes the Green Cycle Start button and the CNC verifies that the vacuum is activated and then moves from the center home position to verify the part is in proper position, once verified by the machine, it will automatically start machining the part on the outboard end of the CNC bed. As this machining is done the operator will position the next part into its position on the Inboard end of the CNC bed. Once the machining is complete the CNC will return to the Center Rest position and release the vacuum on the completed part. The operator will again activate the vacuum on the next part and then push the green Cycle Start button. During machining the operator will remove the previously machined part, do a visual inspection, wiped down, blow off and place on a pallet for shipping for final assembly.
(51) Referring again
(52) The ribs 86, for example three, extend uninterrupted laterally to span the cavity between opposite sides of the perimeter of the rim. As shown in
(53) TABLE-US-00006 TABLE 3 Nominal Load to First Nominal Structural Load Defect Failure Pounds Pounds Version Force Force 1730 with Intersecting Ribs 22,000 29,000 1730 with Laterally Uninterrupted Ribs 30,000 31,000 1730 with Laterally Uninterrupted Added Depth Ribs 33,700 39,000
(54) In addition deeper ribs 86 as shown in
(55) As shown in
(56) The top surface 70 also includes a series of bosses 106 of varying heights to create a gripping surface. The bosses 106 are molded at various heights to allow for aggressive transitions in the surface of the lid. The bosses are arranged in a pattern of alternating groups which allows for additional edge surfaces to grip moving surfaces, such as vehicle tires, which may come in contact with the top of the lid. The bosses create more surface area for flexible materials to come in contact with. The result of the bosses is the surface allows the lid to meet slip resistance requirements. Although
(57) Polymer lid Related Specifications:
(58) The lid is tested to industry recognized standards for: Chemical Resistance Per: Telcordia R3-14 and ASTM D543-06 Ultra Violet Exposure Per: ASTM G154 Fungus Resistance Per: ASTM G21 Flammability Per: UL 94-5 VA and ASTM D635-06 Water Absorption Per: ASTM D570-05
The lid is tested to industry recognized standards for: AS 4586: 2013 Slip resistance classification of new pedestrian surface materials—Appendix A. ANSI/SCTE 77-2010 Specification for Underground Enclosure Integrity, SCTE, 2010 GR-902-CORE, Generic Requirements for Handholes and Other Below-Ground Splice Vaults, Telcordia, 2013 ASTM C857-11, Standard Practice for Minimum Structural Design Loading For Underground Precast Concrete Utility Structures, ASTM, 2011 AS 3996 2006, Access Covers and Grates BS EN 124:1994 Incorporating Amendment No. 1 Gully Tops and manhole tops for vehicular and pedestrian areas—Design requirements, type testing, marking, quality control
(59) As shown in
(60) Referring again to
(61) Other types of fastening mechanisms can be utilized in addition to the L-bolt construction as identified in Applicant's U.S. Pat. No. 7,547,051, the contents of which are incorporated herein by reference in its entirety. Such as, for example, the lid could utilize a self-latching and locking assembly 127 for attachment of the lid to the vault as shown in
(62) As shown in
(63) As shown in
(64) Upon completion of the molding process and ejection of the molded cover from the mold, the robot includes a retractor 152 comprising a plate 154 and series of suction cups 156. The controller opens the press at the correct cycle time and activates the cover ejection mechanism wherein the robot positions the retractor 152 over the molded cover so that the suction cups 156 can engage the cover and move the molded cover to a conveyor system 158 and releases the cover onto the conveyor system. The conveyor system then delivers the molded cover to a machining station 160 which includes a plurality of rotating brushes 162 to deburr the molded cover. The machining station also includes drilling holes for the vault attachment mechanisms.
(65) Final assembly of the cover includes placing the pick hole rod in the recess of the pick hole cup and securing the cup and cap to the lid, securing the identification marker to the lid, securing the L-bolt, through bolt or self-latching mechanism along with the retaining flange and plugging the holes with caps for the attachment mechanisms not used.
(66) Although the invention has been described and illustrated with respect to various embodiments herein, it is to be understood that changes and modifications can be made therein which are within the full intended scope of the invention as hereinafter claimed.