Laminate resin transfer molding of fibrous preforms using particle filled resin systems
10086544 ยท 2018-10-02
Assignee
Inventors
Cpc classification
B29C35/02
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/616
CHEMISTRY; METALLURGY
B29C45/02
PERFORMING OPERATIONS; TRANSPORTING
B29C70/48
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/483
CHEMISTRY; METALLURGY
B29C70/443
PERFORMING OPERATIONS; TRANSPORTING
B29C70/68
PERFORMING OPERATIONS; TRANSPORTING
B29K2083/00
PERFORMING OPERATIONS; TRANSPORTING
C04B35/80
CHEMISTRY; METALLURGY
International classification
B29C45/02
PERFORMING OPERATIONS; TRANSPORTING
C04B35/80
CHEMISTRY; METALLURGY
B29C70/68
PERFORMING OPERATIONS; TRANSPORTING
B29C35/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A process for manufacturing a ceramic matrix composite component, said process comprising inserting at least one fibrous sheet into a resin transfer molding system. The process includes wetting the at least one (dry or partially wetted) fibrous sheet with a neat first pre-ceramic polymer resin. The process includes injecting a second pre-ceramic polymer resin including a filler material into at least one fibrous sheet and curing the pre-ceramic polymer resin.
Claims
1. A resin transfer molding system comprising: a tool having an upper surface; a cover plate coupled with said tool proximate said upper surface; an inner cavity formed between said tool and said cover plate; an intensifier located in said inner cavity and thermally coupled to said tool; a vacuum pump fluidly coupled to said inner cavity; and a pump fluidly coupled to said inner cavity and configured to pump a first neat resin and a second filled resin into said inner cavity.
2. The system according to claim 1, wherein said pump is fluidly coupled to a first resin source and a second resin source.
3. The system according to claim 1, further comprising: a thermal energy subsystem thermally coupled to said tool.
4. The system according to claim 3, further comprising: a seal coupled between said cover plate and said tool and configured to fluidly seal said inner cavity.
5. The system according to claim 1, wherein said first resin comprises a pre-ceramic polymer resin selected from the group consisting of polycarbosilanes and polysilazanes.
6. The system according to claim 1, wherein said second resin comprises a pre-ceramic polymer resin and filler material selected from the group consisting of alpha and beta SiC and B4C.
7. A process for manufacturing a laminate ceramic composite component, said process comprising: inserting at least one fibrous sheet into a resin transfer molding system; wetting said at least one fibrous sheet with a neat first pre-ceramic polymer resin; performing a post injection hold configured to allow for said first pre-ceramic polymer resin to be absorbed into said at least one fibrous sheet; injecting a second pre-ceramic polymer resin into said at least one fibrous sheet, wherein said second pre-ceramic polymer resin comprises filler material; and encapsulating said at least one fibrous sheet and pre-ceramic polymer resin beneath a cover plate, said cover plate being coupled to a tool; encapsulating said at least one fibrous sheet and pre-ceramic polymer resin between a pressure intensifier and said cover plate, wherein said pressure intensifier comprises a cured elastomer having a high coefficient of thermal expansion.
8. The process of claim 7, further comprising: suppressing void formation resultant from gases formed in said pre-ceramic polymer resin.
9. The process of claim 7, further comprising: heating said intensifier to induce a thermal expansion of said intensifier.
10. The process of claim 7, wherein said pre-ceramic polymer resin is selected from the group consisting of polycarbosilanes and polysilazanes.
11. The process of claim 7, further comprising: uniformly applying pressure to the at least one fibrous sheet and pre-ceramic polymer resin to ensure wet out and consolidation.
12. The process of claim 7, wherein said filler material of second pre-ceramic polymer resin is selected from the group consisting of alpha and beta SiC and B4C.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
DETAILED DESCRIPTION
(3) Referring now to
(4) The resin transfer molding system 10 includes a tool 12. The tool 12 can be constructed from composite materials, thin film metals, ceramics or conventional metallic materials. The tool 12 includes a cover plate 14 configured to enclose an upper surface 16 of the tool 12, encapsulate and seal the contents of the tool 12.
(5) Adjacent to the tool 12 is at least one fibrous sheet 18, and shown as multiple sheets 18, which are used to create the composite material. The fibrous sheet can include any dry fabrics, tackified fabrics, prepreg fabrics, three dimensional woven or braided preforms, and other previously formed fiber filled sections.
(6) The sheets 18 are enclosed by the cover plate 14. The cover plate 14 may be constructed from the same rigged material as the tool 12. The cover 28 may also be a flexible bag 20 made of a material, such as nylon, which can be sealed to the tool 12 with a seal 22.
(7) The cover plate 14 and tool 12 define an inner cavity 24. The inner cavity 24 is in fluid communication with a pump 26 configured to pump a resin 28. The pump 26 may be capable of pressurizing the inner cavity 24. The pump 26 can be fluidly coupled to a source of resin 30 and/or a source 32 of the mixture of the resin 28 and a particulate filler material 34, also called a filled resin 32.
(8) The resin 28 is a material which binds and forms a composite with the fibrous material 18 when subjected to elevated temperatures and pressures. In exemplary embodiments, there are thermoset-type or thermoplastic-type pre-ceramic polymer resins. In an exemplary embodiment, the resin 28 is ceramic matrix composite pre-ceramic polymer resin. The resin 28 can include particulate filler material 34. The mixture of resin 28 and filler material 34 together provide greater structural stability and higher ceramic yields. Examples of these pre-ceramic polymer resins include polycarbosilanes and polysilazanes. Fillers can be identified by chemistry; examples are alpha and beta SiC and B4C. The size of the particulate can be varied as well. The particulate can be uniform in size, bimodal in distribution or random.
(9) An optional pressure intensifier 36 can be included in the resin transfer molding system 10. The pressure intensifier 36 comprises a cured elastomer such as silicone rubber material (or functional equivalent) having a high coefficient of thermal expansion that expands when heated. In an exemplary embodiment the coefficient of thermal expansion can be greater than 75 micro in/in Fahrenheit. The pressure intensifier 36 is placed adjacent the upper surface 16 of the tool 12 proximate the fibrous sheets 18. The pressure intensifier 36 is configured to apply pressure to the fibrous sheets 18 and resin 28 upon being heated.
(10) Segregation of the Particulate Filler material during RTM injection is a function of multiple processing, tooling and material variables. One potential mechanism driving segregation at the laminate level is the absorption of the liquid polymer resin 28 into the individual tow bundles of fibrous sheets 18 by capillary action after injection, leaving non-uniform concentrations of filler material 34. In order to mitigate the segregation of the resin 28 and filler material 34, a two-step injection process for RTM of particulate filled preceramic polymer resins can be performed.
(11) The first injection cycle is performed with unfilled (neat) resin 28 at temperatures below the cure temperature of the resin 28 and includes a post-injection hold to allow for absorption of the resin 28 into the tow bundles of fibrous sheets 18. A second injection cycle is then performed with the filled resin 32 to evenly distribute the filler material throughout the intra-tow regions of fibrous sheets 18.
(12) Finally, the resin 28 and filled resin 32 are cured to the green state prior to pyrolysis. The phenomenon that separates the particulate filler 34 from the resin 28 also has been found to leave voids in the laminate as well. The second injection fills these voids.
(13) Referring also to
(14) A vacuum is pulled within the inner cavity 24 of the tool 12 by a vacuum pump 40, at step 160.
(15) At step 180, the neat resin 28 is introduced to the inner cavity 24 from the resin source 30. The resin 28 is neat and has no filler material 34. The temperature of the resin 28 is below the cure temperature of the resin 28. The resin can be induced to flow into the inner cavity 24 by the vacuum created within the tool inner cavity 24, by positively pumping the resin 28 into the inner cavity 24, or both. As shown in
(16) As shown in
(17) A post resin 28 injection hold is performed at step 200. The hold allows for the neat resin 28 to be absorbed into the fibrous sheets 18. The period of time for the hold can vary, but in an exemplary embodiment, a time range of from 5 minutes to 1 hour can be employed.
(18) At step 220, a second injection cycle is performed. The filled resin 32 comprising a mixture of resin 28 and filler material particles 34 is introduced to the inner cavity 24 from the filled resin source 32. The resin 28 has filler material 34. The filler material 34 is evenly distributed throughout the intra-tow regions/gaps 42.
(19) Optionally, the tool 12 is heated from the thermal energy subsystem 38. The heat Q from the thermal energy subsystem 38 transfers through the tool 12 into the pressure intensifier 36. As the intensifier 36 is heated, the intensifier 36 expands and presses the sheets 18 and resin 28 within the mold cavity. In an exemplary embodiment, the intensifier 36 can apply a pressure of from about 50 pounds per square inch (psi) to as high as 800 psi. Other means of exerting pressure on the sheets 18 can also be deployed.
(20) As explained above, prior to, during and even after initial cure the pre-ceramic resins 28 have demonstrated a propensity for release of gaseous compounds. These gases can interfere with the complete filling of the fiber preform during resin injection, leading to a cured laminate with varying amounts, sizes and shapes of porosity.
(21) The use of pressure, developed through the implementation of an intensifier or by other means 30, suppresses the formation and release of the gaseous compounds in the laminate formed from the resin 28 and fibrous sheets 18. By suppressing the outgassing of the resin 28, unwanted voids and the resultant porosity is avoided in the composite material component. The second injection 220 of the two step injection cycle, serves to fill any voids that may remain in the composite material component.
(22) Optionally, at step 240, the resins 28/32 are cured to the green state prior to pyrolysis.
(23) Using the ceramic matrix composite pre-ceramic polymer resin with the RTM process can result in large voids and defects in the cured laminate that propagate to the pyrolyzed laminate during PIP and are not filled during final densification. The disclosed resin transfer molding system enables one to cure a laminate by RTM using pre-ceramic polymer resin such that large pores are not present and the gas/porosity evolution is either suppressed or results in very small, finely dispersed porosity.
(24) For final densification various processes can be employed such as; PIP, Melt Infiltration (MI) or Chemical Vapor Infiltration (CVI).
(25) The resin transfer molding system and method (or functionally equivalent method) can be applicable to flat panels as well as complex 3-D geometric shapes including those forming functional components.
(26) The exemplary resin transfer molding system is a closed tool process in which a dry or partially wetted fiber preform is enclosed in matched metal tooling and resin is injected under pressure to wet out the preform. The tool is then heated to cure the resin, resulting in a composite laminate. The closed tooling creates a dimensionally repeatable part.
(27) Uniform Distribution of Particulate Filler material and complete wetting of the laminate volume, both inter-tow and intra-tow, in the green state CMC laminate will produce a stable laminate after pyrolysis with uniform, predictable matrix shrinkage cracks. This behavior is beneficial to subsequent re-infiltrations, including final densification via CVI, as well as modeling techniques for analytical behavior prediction.
(28) By preventing segregation of filler material and minimizing the voids developed during cure, the exemplary system and method allow for the successful densification of the laminate through processes such as Polymer Infiltration and Pyrolysis (PIP), Melt Infiltration (MI) or Chemical Vapor Infiltration (CVI). A highly dense material is critical to the durability of the material.
(29) Without the use of the exemplary resin transfer molding system and method a more porous Ceramic Matrix Composite (CMC) can result, the greater porosity compromising the composite and the capacity of the composite to meet target life requirements and ultimately increasing cost.
(30) There has been provided a resin transfer molding system and process. While the resin transfer molding system and process have been described in the context of specific embodiments thereof, other unforeseen alternatives, modifications, and variations may become apparent to those skilled in the art having read the foregoing description. Accordingly, it is intended to embrace those alternatives, modifications, and variations which fall within the broad scope of the appended claims.