WO2000046015A1 - Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure - Google Patents
Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure Download PDFInfo
- Publication number
- WO2000046015A1 WO2000046015A1 PCT/US2000/003152 US0003152W WO0046015A1 WO 2000046015 A1 WO2000046015 A1 WO 2000046015A1 US 0003152 W US0003152 W US 0003152W WO 0046015 A1 WO0046015 A1 WO 0046015A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- resin
- vacuum
- fluid
- pressure
- bag
- Prior art date
Links
- 239000011347 resin Substances 0.000 title claims abstract description 110
- 229920005989 resin Polymers 0.000 title claims abstract description 110
- 239000012779 reinforcing material Substances 0.000 title claims abstract description 10
- 238000000034 method Methods 0.000 title claims description 62
- 238000005470 impregnation Methods 0.000 title description 5
- 239000012530 fluid Substances 0.000 claims abstract description 62
- 239000000463 material Substances 0.000 claims abstract description 26
- 238000004519 manufacturing process Methods 0.000 claims abstract description 10
- 238000007789 sealing Methods 0.000 claims abstract description 5
- 238000001816 cooling Methods 0.000 claims description 3
- 238000003825 pressing Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 1
- 239000012778 molding material Substances 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 abstract 2
- 238000001802 infusion Methods 0.000 description 31
- 239000000758 substrate Substances 0.000 description 28
- 239000000835 fiber Substances 0.000 description 21
- 230000033001 locomotion Effects 0.000 description 7
- 239000004033 plastic Substances 0.000 description 7
- 229920003023 plastic Polymers 0.000 description 7
- 239000002131 composite material Substances 0.000 description 6
- 238000012546 transfer Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000001721 transfer moulding Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229920002430 Fibre-reinforced plastic Polymers 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 239000003733 fiber-reinforced composite Substances 0.000 description 4
- 239000011151 fibre-reinforced plastic Substances 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000004744 fabric Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 230000002787 reinforcement Effects 0.000 description 3
- 239000004677 Nylon Substances 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000005056 compaction Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011152 fibreglass Substances 0.000 description 2
- 229910002804 graphite Inorganic materials 0.000 description 2
- 239000010439 graphite Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 229920001778 nylon Polymers 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 230000003014 reinforcing effect Effects 0.000 description 2
- 239000012783 reinforcing fiber Substances 0.000 description 2
- 239000011800 void material Substances 0.000 description 2
- 239000003039 volatile agent Substances 0.000 description 2
- 241000905957 Channa melasoma Species 0.000 description 1
- 229920000271 Kevlar® Polymers 0.000 description 1
- 229920012266 Poly(ether sulfone) PES Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 238000007792 addition Methods 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000007596 consolidation process Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000002657 fibrous material Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 230000009969 flowable effect Effects 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000004761 kevlar Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000002990 reinforced plastic Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- KKEYFWRCBNTPAC-UHFFFAOYSA-L terephthalate(2-) Chemical compound [O-]C(=O)C1=CC=C(C([O-])=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-L 0.000 description 1
- 229920006345 thermoplastic polyamide Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C70/00—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts
- B29C70/04—Shaping composites, i.e. plastics material comprising reinforcements, fillers or preformed parts, e.g. inserts comprising reinforcements only, e.g. self-reinforcing plastics
- B29C70/28—Shaping operations therefor
- B29C70/40—Shaping or impregnating by compression not applied
- B29C70/42—Shaping or impregnating by compression not applied for producing articles of definite length, i.e. discrete articles
- B29C70/44—Shaping or impregnating by compression not applied for producing articles of definite length, i.e. discrete articles using isostatic pressure, e.g. pressure difference-moulding, vacuum bag-moulding, autoclave-moulding or expanding rubber-moulding
- B29C70/443—Shaping or impregnating by compression not applied for producing articles of definite length, i.e. discrete articles using isostatic pressure, e.g. pressure difference-moulding, vacuum bag-moulding, autoclave-moulding or expanding rubber-moulding and impregnating by vacuum or injection
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
- B29C35/0227—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using pressure vessels, e.g. autoclaves, vulcanising pans
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C35/00—Heating, cooling or curing, e.g. crosslinking or vulcanising; Apparatus therefor
- B29C35/02—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould
- B29C35/04—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using liquids, gas or steam
- B29C35/041—Heating or curing, e.g. crosslinking or vulcanizing during moulding, e.g. in a mould using liquids, gas or steam using liquids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C2791/00—Shaping characteristics in general
- B29C2791/004—Shaping under special conditions
- B29C2791/006—Using vacuum
Definitions
- the present invention relates to resin impregnated fiber composites and more particularly to a manufacturing process for manufacturing resin impregnated fiber composites utilizing fluid to apply pressure to the composite .
- Fiber reinforced composite parts are fabricated utilizing a variety of conventional techniques including vacuum resin infusion, resin transfer molding (RTM) , prepreg/autoclave procedures, and compression molding operations.
- Vacuum resin infusion consists of infusing a preform with liquid resin under vacuum using a one sided tool.
- Resin transfer molding differs from vacuum resin infusion by infusing the preform with liquid resin under pressure with or without vacuum using a matched, two sided tool capable of withstanding the pressure.
- Fiber reinforced plastic structures have been commercially produced for some years. Examples of manufacturing techniques can be found in US Patent No.
- Reinforcing fiber generally takes the form of one or more layers of a woven or felted fiber reinforcement, typically comprised of carbon, graphite, or fiberglass.
- the vacuum resin infusion or impregnation process is usually done by either a wet or dry fiber lay-up technique.
- the resin "wetted" fiber reinforcement consists of a prepreg which already contains a resin and is laid up on a mold and cured.
- the fiber reinforcement is laid up dry on a mold or form which serves as a mold.
- the form may be incorporated as part and parcel of the finish product.
- the fiber is sprayed, brushed, impregnated, infused, or otherwise coated or "wetted" with the resin.
- the resin is then cured to form the fiber reinforced plastic structure.
- the structure can be placed in a vacuum to assist the curing process.
- vacuum bag techniques have been used to provide such vacuum assistance.
- a vacuum technique a flexible impervious sheet, liner, or bag is used to cover a single mold which contains the dry or wet (resin impregnated) fiber lay- up.
- wet fiber process the edges of the flexible sheet are clamped against the mold to form an envelope and seal the resin impregnated fiber lay-up to the mold and out of the atmosphere.
- a vacuum is then applied to consolidate, the preform during the cure of the resin.
- catalyzed liquid plastic or resin is generally introduced into the envelope or bag interior to wet the dry fiber, usually using a vacuum (usually applied before resin introduction) to help push the resin into the bag and wet out the dry fiber.
- Vacuum is applied to the bag interior via a vacuum line to collapse flexible sheet against the fiber and surface of the mold, and then the plastic wetted fiber is processed, compacted and cured to form the fiber reinforced structure.
- the vacuum bag used in this process is critical because it provides a. vacuum seal and consolidation pressure .
- Prior vacuum resin infusion processes have had a number of problems when fabricating a large part.
- the maximum part height (h, ⁇ ) is about 33 ft., assuming a minimum resin density (p) of 1.03 grams per cm 3 .
- Methods to overcome this 33 ft. limitation such as multi-stage infusions, may be undesirable because the stage boundaries are subject to property variations.
- Another technique to overcome the 33 ft. limitation is to use pressurized injection. This may be undesirable however because of the risk of inflating the bag, or the cost associated with rigid matched tools.
- vacuum resin infusion processes have typically been slow proportionally as the effective vacuum resin infusion pressure decreases as a function of height. Slow filling increases the risk of resin gelation before completing the infusion. Therefore, the risk of having a bad part increases as a function of height, especially above 20 ft..
- part height limits processing options such as "final vacuum". After filling with a high vacuum (>27" Hg) , it is desirable to reduce the final vacuum to minimize porosity and control resin content. If the final vacuum is too high, the volatiles within the resin are more likely to boil, creating undesirable porosity. Also, high vacuum tends to yield low resin contents, which may be undesirable for some applications .
- Another problem with prior vacuum resin infusion processes is that the effective processing pressure varies as a function of height per the formula pgh . This pressure ingredient yields property variations, such as resin content as a function of height. Resin content variations yield variations in strength, modulus, toughness and specific gravity of the final part and are therefore undesirable.
- An object of the present invention is to provide a vacuum resin infusion process for a composite article which provides fluid pressure on the article.
- Another object of the present invention is to provide a vacuum resin infusion process for a composite article which provides fluid pressure on the article while providing controlling temperature.
- a method of manu acturing a resin impregnated reinforced article comprising the steps of providing a permeable reinforcing material on a mold, sealing the material with a flexible, impervious sheet, introducing resin into the material, drawing a vacuum on the material within the sealed sheet, applying pressure on the flexible sheet and material with a fluid in contact with the impervious sheet.
- a method of manuf cturing a resin impregnated reinforced article comprising the steps of providing a permeable reinforcing material on a mold, sealing the material with a flexible, impervious sheet, introducing resin into the material, drawing a vacuum on the material within the sealed sheet, applying pressure on the flexible sheet and material with a fluid in contact with the impervious sheet, and controlling the temperature of the fluid.
- the present invention provides a cost effective resin infusion process which permits the manufacture of parts with unlimited height while minimizing resin variations and the porosity of the finished part.
- the present invention also minimizes mechanical and physical degradation, thermal shrinkage gradients, residual stresses, and cracking.
- the present invention accelerates processing time.
- Fig. 1 is a simplified schematic diagram of a vacuum resin infusion process in accordance with the present invention.
- Fig. 2 is a simplified schematic diagram of a vacuum resin infusion process in accordance with an alternative embodiment of the present invention.
- Fig. 3 is a simplified schematic diagram of a vacuum resin infusion process in accordance with an alternative embodiment of the present invention.
- Fig. 4 is a simplified schematic diagram of a vacuum resin infusion process in accordance with an alternative embodiment of the present invention.
- a vacuum resin infusion process in accordance with the present invention, there is shown a mold 110 (or tool or film layer, etc.) in which a permeable fibrous reinforcing substrate 112 is to be placed to form a finished part.
- the mold is preferably a durable material with the appropriate amount of rigidity.
- the shape of the mold determines the shape of the finished part, and thus the mold can be curved or of any desired shape.
- the substrate is preferably comprised of a permeable, reinforced fibrous material such as a laminate or preformed cloth which is placed on top of the mold.
- Other types of reinforcing material structures known in the art, such as woven roving mat, continuous roving mat, or chopped mat may be used instead of or in addition to cloth.
- chopped fibers, continuous roving or certain agate fillers can also be used for this laminate if desired.
- the material for the reinforcing cloth or fibers may be any of a number of known materials that are utilized for vacuum resin transfer molding purposes, such as carbon, fiberglass, kevlar, nylon, graphite, or the like.
- a sheet 114 of flexible, impermeable bag material is placed over the top of the substrate 110 and sealed to the mold around the substrate so as to seal the substrate within a chamber.
- An adhesive such as tacky tape strips (not shown) may be utilized for the sealing purpose.
- a vacuum line 116 provides access to the area between the impermeable bag 114 and the substrate 110. Vacuum is applied utilizing a vacuum controller 118.
- a line 120 provides access to the area between the substrate 112 and the mold 110 at the bottom of the mold.
- a resin source or controller 122 provides resin through line 122 to the substrate 112.
- a fluid 126 is provided in contact with bag 114.
- the fluid is provided in the well created by the shape of the mold and substrate.
- a fluid controller 128 provides a fluid via lines 130, 132 and may control such things as the motion or movement of the fluid (to improve heat transfer) , the pressure applied to the bag and the temperature of the fluid and bag. Fluid motion and pressure may be controlled using devices such as a pump or mixer.
- a lid or cap 138 may be placed over the top of the mold 110 to thereby seal the chamber 140.
- a pressure controller 142 can be utilized to control the pressure within the mold chamber 140 via a line 144.
- the process for impregnating the fibrous pre-form 112 according to the invention illustrated in Fig. 1 is to first apply the substrate 112 to the mold 110.
- the resin and vacuum lines 120 and 116 are secured over the substrate.
- the impervious vacuum bag 114 is disposed over the substrate, and the bag is sealed to the mold around the substrate.
- the bag is then evacuated utilizing the vacuum controller 118.
- a vacuum of about at least 27" Hg is preferred.
- the bag should be free of leaks.
- the bagged preform is then immersed with a fluid, (such as water) to the desired height h*.
- the preform is protected from the fluid with the impervious vacuum bag.
- the fluid applies extra compaction pressure to the laminate. Water is the preferred fluid, although other fluids may be used to accomplish the objectives of the present invention.
- the resin line 120 is placed in a resin reservoir 122 which is below the highest point of the fluid. Fluid pressure prevents the bag from inflating, even when injecting resin under pressure so that the resin reservoir may be placed near the highest point of the mold to apply maximum infusion pressure. High infusion pressure accelerates resin flow, which minimizes infusion time.
- the resin line is then opened and the pre-form is infused with the resin.
- the water reservoir equalizes the pressure as a function of height because both the water pressure and the effective resin pressure vary as a function of pgh. If the fluid's specific gravity simulates the resin's specific gravity, the effective pressure will be constant across the entire height. The process of the present invention is therefore not limited by the height of the part. Some applications may require to keep the resin reservoir at the lowest point and inject the resin under pressure.
- the amount of pressure introduced by the resin is a function of the height of the resin according to the equation P R -P R ⁇ R were p R is the density of the resin and h R is the height of the resin.
- the pressure exerted by the fluid is determined by the equation
- a pressure controller 142 can introduce pressure into the sealed compartment via line 144 if the compartment 140 is sealed, such as by a lid or cap 138.
- resin controller 122 could provide the resin under pressure utilizing forces other than gravity (such as with a pump or other means) .
- resin could not be introduced under pressure because it would cause the impermeable bag to inflate.
- controlling the temperature of the fluid provides heat transfer in order to help control the temperature of the reaction.
- fluid controller 128 can adjust the temperature of the fluid 126 such that the substrate can be cured without having to move it to a different facility, such as an autoclave.
- the fluid controller can work in any of a number of different manners, such as to have the fluid flow through the controller via a pump such that the fluid is circulating in the reservoir.
- the fluid controller may also include a coil or element type temperature controller which either is cooled or heated according to the desired process temperature.
- a fiber substrate 212 is placed on a mold 210.
- a fluid impervious bag 214 is placed over the substrate 212 and sealed to the mold.
- a second fluid impervious bag 215 is placed over the first bag 214 and sealed.
- a vacuum controller 218 provides a vacuum via a line 216 to the area between the first bag 214 and the substrate 212.
- a resin controller 222 introduces resin via a line 220 into the substrate 212.
- a fluid controller 228 provides a fluid v a lines 230, 232 in the space between bag 214 and 215 and may control such things as the motion of the fluid (to improve heat transfer) , the pressure applied to the bag and the temperature of the bag. Fluid motion and pressure may be controlled using devices such as a pump or mixer.
- An additional layer 217 may be disposed between bag 214 and bag 215 and may be textured for providing channels for resin to flow through during the infusion of the resin, and channels for the fluid to flow during and/or after the infusion of the resin.
- a vacuum is created via vacuum controller 218 via line 216.
- the vacuum removes air from the cavity or envelope 213 and collapses the bags 214, 215.
- the pressure differential across the envelope 213 pulls resin from resin source or controller 222 through line 220. Resin will thereafter flow from the bottom of the molds 210 to the top of the substrate and impregnate the pre-form 212 with the resin material.
- Fluid controller 228 controls the motion, pressure and temperature of fluid located between the inner bag 214 and the outer bag 215 during the curing process.
- an alternative embodiment of a vacuum resin infusion process in accordance with the present invention includes the use of a tool 310 on which a laminate or substrate 312 is placed.
- An impermeable bag 314 is placed and sealed over the substrate 312, leaving a void 313 provided therebetween.
- a vacuum controller 318 provides a vacuum in the space 313 via a line 316.
- a resin source or controller 322 provides a resin to the laminate 312 via a line 317.
- the tool 310, substrate 312, and bag 314 are placed in a container 350 filled with a fluid 326.
- An additional, textured layer such as bubble wrap, may be disposed between bag 314 and substrate 312 for providing channels for resin to flow through during the infusion of the resin, and channels for the fluid to flow during and/or after the infusion of resin.
- a fluid controller 328 controls the fluid 326 via lines 330, 332 and may control such things as the pressure, motion or circulation of the fluid (to improve heat transfer) and the temperature of the fluid.
- a pressure controller 342 controls the pressure inside the container 350 via a line 344.
- a lid or cap 338 can be placed over the container in order to more effectively control the pressure within the container.
- an alternative embodiment of a vacuum resin infusion process in accordance with the present invention includes the use of a tool 410 on which a laminate or substrate 412 is placed. An impermeable bag 414 is placed and sealed over the substrate 412, leaving a void 413 provided therebetween.
- a vacuum controller 418 provides a vacuum in the space 413 via a line 416.
- a resin source or controller 422 provides a resin to the laminate 412 via a line 417.
- An additional, textured layer such as bubble wrap, may be disposed between bag 414 and substrate 412 for providing channels for resin to flow through during the infusion of the resin.
- a fluid controller 428 sprays or pours a fluid 415 on the surface of the impermeable bagging material in order to control the temperature of the curing process. This method, however, does not lend itself to as accurate control of the temperature as the previously described methods.
- An example of a variation in the present process would be to vary the temperature of the fluid during the course of the manufacturing process.
- the fluid can be kept lower in order to draw heat from the part.
- the temperature of the fluid can be raised to further cure the part in order to increase the glass transition temperature, strength and stiffness of the part. With the appropriate fluid and pressure, the temperature can be raised significantly for this post bake or curing process.
- the molds and tools of the present invention are preferably made from a rigid or semi-rigid, wear resistant material which is easily cleaned of all resin residue.
- Such mold materials are well known in the art and include metals, plastic, reinforced plastics, etc..
- the bagging materials may be any of a number of suitable materials known to those skilled in the art, such as thermoplastic polyamide films, polyurethane, nylon, polyethylene, terephthalate (PET) , polyether keytone (PEEK), polyetheri ide (PEI), polyether sulfone (PES), etc..
- the present invention allows uniform pressure on the part throughout the height of the part, without the need for costly rigid tooling.
- the present invention provides laminate compaction in excess of 14.7 psi without an autoclave or matched tooling.
- the present invention also provides for a low cost temperature control without the need for expensive cooling systems to the mold. To this end, previous molds with cooling or temperature control could only control the temperatures on the mold surface of thick laminates. The bag side of thick parts, however, heretofore had higher porosity than the mold surface.
- the thermal control provided by the present invention offers an effective way to prevent this.
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- Physics & Mathematics (AREA)
- Health & Medical Sciences (AREA)
- Oral & Maxillofacial Surgery (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Composite Materials (AREA)
- Mechanical Engineering (AREA)
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
Description
Claims
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU29848/00A AU747633B2 (en) | 1999-02-05 | 2000-02-07 | Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure |
CA002358898A CA2358898C (en) | 1999-02-05 | 2000-02-07 | Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure |
DE60002667T DE60002667D1 (en) | 1999-02-05 | 2000-02-07 | METHOD FOR IMPRAINING RESIN FROM RESIN BY VACUUM SUCTION WITH PRESSURE COMPENSATION |
JP2000597115A JP3904833B2 (en) | 1999-02-05 | 2000-02-07 | Vacuum assisted resin impregnation method for reinforcing materials using uniform pressure |
EP00908521A EP1150827B1 (en) | 1999-02-05 | 2000-02-07 | Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/245,524 US6537483B1 (en) | 1999-02-05 | 1999-02-05 | Pressure equalized vacuum resin infusion process |
US09/254,524 | 1999-02-05 |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2000046015A1 true WO2000046015A1 (en) | 2000-08-10 |
WO2000046015A9 WO2000046015A9 (en) | 2001-06-14 |
Family
ID=22927027
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2000/003152 WO2000046015A1 (en) | 1999-02-05 | 2000-02-07 | Process for the vacuum-assisted resin impregnation of reinforcing material with equalized pressure |
Country Status (7)
Country | Link |
---|---|
US (1) | US6537483B1 (en) |
EP (1) | EP1150827B1 (en) |
JP (1) | JP3904833B2 (en) |
AU (1) | AU747633B2 (en) |
CA (1) | CA2358898C (en) |
DE (1) | DE60002667D1 (en) |
WO (1) | WO2000046015A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1277563A1 (en) * | 2001-07-18 | 2003-01-22 | Klaus Dr.-Ing. Wenderoth | Method and apparatus for manufacturing moulded bodies |
WO2007003011A1 (en) * | 2005-07-05 | 2007-01-11 | Quickstep Technologies Pty Ltd | Composite component production using fluid density and pressure |
US8002926B2 (en) | 2005-03-22 | 2011-08-23 | Quickstep Technologies Pty Ltd. | Composite tube production |
US8580176B2 (en) | 2001-01-25 | 2013-11-12 | Quickstep Technology Pty Ltd. | Method of producing composite or bonded metal components |
US8741092B2 (en) | 2000-03-03 | 2014-06-03 | Quickstep Technologies Pty Ltd. | Production, forming, bonding, joining and repair systems for composite and metal components |
Families Citing this family (25)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7413694B2 (en) * | 1999-12-07 | 2008-08-19 | The Boeing Company | Double bag vacuum infusion process |
US6660214B2 (en) * | 2001-02-23 | 2003-12-09 | Essef Corporation | Pressure vessel manufacture method |
DE10252633A1 (en) * | 2002-05-27 | 2003-12-11 | Kmb Produktions Ag Felben | Method and device for producing consumer goods |
GB2403179B (en) * | 2003-06-24 | 2007-10-24 | Trysome Ltd | Liquid supply system |
US7442337B2 (en) * | 2004-04-30 | 2008-10-28 | Medtronic, Inc. | Method of laminating articles |
US8066503B2 (en) * | 2005-10-25 | 2011-11-29 | The Boeing Company | Controlled delta pressure bulk resin infusion system |
US7758800B2 (en) * | 2005-12-22 | 2010-07-20 | Comtek Advanced Structures Limited | System and method for resin infusion |
US8034278B2 (en) * | 2006-01-13 | 2011-10-11 | Hexcel Corporation | Pressurized molding of composite parts |
FR2897291B1 (en) * | 2006-02-14 | 2012-05-04 | Chomarat Composites | BASKET FOR CLOSING A MOLDING MOLD BY FULLY MOLDED TECHNIQUE, AND IN PARTICULAR BY INFUSION OR INJECTION OF RESIN |
US7862322B2 (en) * | 2006-04-25 | 2011-01-04 | Florida State University Research Foundation | Resin infusion between double flexible tooling system |
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US8741092B2 (en) | 2000-03-03 | 2014-06-03 | Quickstep Technologies Pty Ltd. | Production, forming, bonding, joining and repair systems for composite and metal components |
US8580176B2 (en) | 2001-01-25 | 2013-11-12 | Quickstep Technology Pty Ltd. | Method of producing composite or bonded metal components |
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US8002926B2 (en) | 2005-03-22 | 2011-08-23 | Quickstep Technologies Pty Ltd. | Composite tube production |
WO2007003011A1 (en) * | 2005-07-05 | 2007-01-11 | Quickstep Technologies Pty Ltd | Composite component production using fluid density and pressure |
Also Published As
Publication number | Publication date |
---|---|
WO2000046015A9 (en) | 2001-06-14 |
JP3904833B2 (en) | 2007-04-11 |
US6537483B1 (en) | 2003-03-25 |
JP2003525141A (en) | 2003-08-26 |
DE60002667D1 (en) | 2003-06-18 |
AU747633B2 (en) | 2002-05-16 |
CA2358898A1 (en) | 2000-08-10 |
EP1150827B1 (en) | 2003-05-14 |
AU2984800A (en) | 2000-08-25 |
EP1150827A1 (en) | 2001-11-07 |
CA2358898C (en) | 2006-05-02 |
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