US20170036378A1 - Foaming technology in long glass fiber filled materials - Google Patents

Foaming technology in long glass fiber filled materials Download PDF

Info

Publication number
US20170036378A1
US20170036378A1 US15/304,059 US201515304059A US2017036378A1 US 20170036378 A1 US20170036378 A1 US 20170036378A1 US 201515304059 A US201515304059 A US 201515304059A US 2017036378 A1 US2017036378 A1 US 2017036378A1
Authority
US
United States
Prior art keywords
long glass
foamed
foamed part
glass fibers
equal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
US15/304,059
Other languages
English (en)
Inventor
Angel Yanev
Marnik Vaes
Warden Schijve
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SABIC Global Technologies BV
Original Assignee
SABIC Global Technologies BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by SABIC Global Technologies BV filed Critical SABIC Global Technologies BV
Priority to US15/304,059 priority Critical patent/US20170036378A1/en
Assigned to SABIC GLOBAL TECHNOLOGIES B.V. reassignment SABIC GLOBAL TECHNOLOGIES B.V. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: VAES, MARNIK, SCHIJVE, WARDEN, YANEV, Angel
Publication of US20170036378A1 publication Critical patent/US20170036378A1/en
Abandoned legal-status Critical Current

Links

Images

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
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/0005—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor using fibre reinforcements
    • 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
    • B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34—Auxiliary operations
    • B29C44/36—Feeding the material to be shaped
    • B29C44/38—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length
    • B29C44/42—Feeding the material to be shaped into a closed space, i.e. to make articles of definite length using pressure difference, e.g. by injection or by vacuum
    • 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
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17—Component parts, details or accessories; Auxiliary operations
    • B29C45/18—Feeding the material into the injection moulding apparatus, i.e. feeding the non-plastified material into the injection unit
    • 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
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/17—Component parts, details or accessories; Auxiliary operations
    • B29C45/1703—Introducing an auxiliary fluid into the mould
    • B29C45/1704—Introducing an auxiliary fluid into the mould the fluid being introduced into the interior of the injected material which is still in a molten state, e.g. for producing hollow articles
    • B29C2045/1722—Introducing an auxiliary fluid into the mould the fluid being introduced into the interior of the injected material which is still in a molten state, e.g. for producing hollow articles injecting fluids containing plastic material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/04—Condition, form or state of moulded material or of the material to be shaped cellular or porous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/06—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts
    • B29K2105/12—Condition, form or state of moulded material or of the material to be shaped containing reinforcements, fillers or inserts of short lengths, e.g. chopped filaments, staple fibres or bristles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2309/00—Use of inorganic materials not provided for in groups B29K2303/00 - B29K2307/00, as reinforcement
    • B29K2309/08—Glass
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2509/00—Use of inorganic materials not provided for in groups B29K2503/00 - B29K2507/00, as filler
    • B29K2509/08—Glass

Definitions

  • Certain formed polymeric parts e.g., automotive parts, are continually desired to be lighter in weight without a reduction in mechanical or physical properties of the part.
  • Foamed injection molding can provide a lighter weight part as compared to a part formed by other methods, but using foamed injection molding with long glass fiber filled materials can result in fiber breakage with intrinsic loss of mechanical properties such as strength, stiffness, and impact resistance.
  • a method of making a foamed part comprises: introducing a long glass fiber filled polymeric material to a hopper of an injection molding machine, wherein the long glass fibers have a pre-molding length; melting the long glass fiber filled polymeric material to form a melt; pressurizing a plasticizing unit of the injection molding machine with a blowing agent, wherein a seal is located between a rotating part and a fixed part of the plasticizing unit; having a seal between the rotating and fixed parts of the plasticizing unit; sealing the plasticizing unit with an airlock mounted between a barrel of the injection molding machine and the hopper; increasing a pressure of the blowing agent and increasing a back pressure of the injection molding machine to homogenize the melt and the blowing agent; and forming the foamed part; wherein a post-molding length of the long glass fibers in the foamed part is greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned foamed part made without the pressurized plasticizing unit.
  • a foamed part comprises: a long glass fiber filled polymeric material, wherein the long glass fibers have an initial length before molding of the foamed part and a final length after molding of the foamed part; wherein a post-molding length of the long glass fibers in the foamed part is greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned foamed part made without a pressurized plasticizing unit.
  • FIGS. 1A to 1F are pictures of cut sections of foamed plaques showing the cell structure and density with a 30% weight reduction.
  • FIGS. 2A to 2F are pictures of cut sections of foamed plaques showing the cell structure and density with a 20% weight reduction.
  • FIG. 3A to 3C are pictures of a foamed plaque illustrating positions where cut sections of the cell structure via light microscopy and density measurements were taken.
  • FIGS. 4A and 4B are pictures of a foamed plaque illustrating positions where light microscopy was performed on decompression samples.
  • FIGS. 5A to 5D are pictures of a cut section of the foamed plaque with 2.3 times the original thickness molded with Composition No. 2.
  • FIGS. 6A and 6B are pictures of a cut section of the foamed plaque with 4 times the original thickness molded with Composition No. 5.
  • FIG. 7 is a graphical illustration of fiber length measurements in the molded parts.
  • FIG. 8 is a graphical illustration of the number of long fibers in the molded parts made by solid injection molding and made by foaming injection molding.
  • FIG. 9 is a graphical illustration of the ash content in solid and foamed parts.
  • FIG. 10 is a graphical illustration of the flow length versus density of molded parts as described herein.
  • FIGS. 12A-12D are graphical illustrations of the flexural strength of various molded samples as described herein.
  • FIGS. 13A and 13B are graphical illustrations of the impact strength of various molded samples as described herein.
  • FIGS. 14A and 14B are graphical illustrations of the impact strength of displacement molded samples as described herein.
  • the foamed part can be made from a long glass fiber filled polymeric material.
  • the long glass fibers can have an initial length before molding of the foamed part and a final length after molding of the foamed part.
  • the final length of the long glass fibers in the foamed part is greater than or equal to a final length of long glass fibers in a non-foamed part.
  • certain mechanical properties such as strength, stiffness, and impact resistance can be comparable to non-foamed (e.g., solid) parts, with a reduction in weight as compared to solid parts.
  • the technology used to manufacture parts from long glass fiber filled materials such that an average fiber length in the final part can be reduced by less than a reduction in an average fiber length in the final part made by other foaming technologies can include placing an injection screw under pressure with a relatively flat pressure profile. Such a manufacturing process can help ensure the long glass fibers do not break during the forming process.
  • Foaming technologies such as the use of a chemical blowing agent or physical foaming agent, can lead to excessive fiber breakage, which directly affects the mechanical and physical properties of a part made with these methods using a long glass fiber filled material. Consequently, performance enhancements observed by using long glass fiber filled materials, instead of short glass fiber filled materials can be erased.
  • Long glass fiber breakage can occur due to shear stress applied during the homogenization phase of the process where the gas, (whether coming from a chemical or physical blowing agent), is homogenized with the molten polymeric material. If the glass fiber length can be held constant, or even increased, as compared to other processes, during the injection foaming process, the reduction of properties, including impact resistance, due to foaming, can be minimized and even further weight reduction in the resulting part can be achieved.
  • foaming agents in polymeric materials can reduce density and thus, also reduce weight of a final part.
  • Foam molding can offer the possibility of increasing the size of a part without increasing the weight and reducing the weight of a part with a controlled change in properties.
  • Other valuable advantages for foaming are cycle time reduction, improved dimensional uniformity, and increased cavitation in a mold.
  • the gas is generated by chemical decomposition of a blowing agent.
  • the blowing agent is added as a masterbatch system.
  • the decomposition is initiated by heat of the melt during plasticizing.
  • Endothermic foaming agents are mainly used for injection molding. They are based on bicarbonate and citric acid substances.
  • Chemical foaming involves mixing a chemical blowing agent with pellets prior to the pellets being fed into the feed throat of an injection molding machine.
  • the blowing agent decomposes while the resin is melting, releasing a gas such as nitrogen that is mixed with the polymer.
  • Endothermic foaming agents can be used for injection molding.
  • the endothermic foaming agents can be based upon bicarbonate and citric acid substances. As the polymer is injected into the mold, the gas expands.
  • the bubbles formed help pack the resin in the mold.
  • Chemical foaming can be done on any existing molding machine with the only restriction that a blowing agent be used that decomposes at a temperature compatible with the processing temperature of the polymer.
  • Using chemical foaming with long glass fiber filled polymeric materials can result in a reduction in the long glass fibers of about 20% as compared to solid injection molding (i.e., non-foamed injection molding), due to an increase in back pressure applied for homogenization of the melt during the plastification stage of the process.
  • decompression technology can be applied. Decompression refers to increasing the part thickness by opening the mold immediately after filling the cavity.
  • Foaming can be started using standard injection molding conditions for the resin being molded.
  • pack pressure and/or packing time should be changed. A decrease in packing will increase foaming and an increase in packing will decrease foaming. Setting the stroke to produce a short shot will also increase the amount of foaming. It can also be desirable to adjust the level of foaming agent used, the melt temperature being used, or the type of foaming agent used. Faster cycle times can be achieved by reducing the packing time. This is possible since the gas pressure in the part is actually packing the part and not hydraulic pressure.
  • Physical foaming can be achieved by adding a gas such as nitrogen, oxygen, or carbon dioxide within a defined pressure and temperature range to the polymer melt and generally requires a special screw design with mixing elements located in front of the screw. Within this range the gas becomes a supercritical fluid and can be dissolved within the polymer melt during plasticizing.
  • a gas such as nitrogen, oxygen, or carbon dioxide
  • Various techniques can be used to add the gas to the melt as a supercritical fluid, including adding the gas to the melt in the machine barrel (technique 1) and adding the gas to the melt in an adapted hot runner system (technique 2).
  • Technique 1 involves metering a gas such as nitrogen into the polymer melt stream as it moves down the barrel.
  • the gas is thoroughly mixed into the polymer creating a single phase solution of polymer and gas.
  • Nucleation from the pressure drop of the resin being injected into the mold causes gas bubble formation and cell growth occurs while the part cools, packing the resin into the mold like chemical foaming.
  • special gas delivery equipment needs to be purchased and the injection molding machine needs to be modified.
  • mixing elements are located in front of the screw. These mixing elements cause severe glass fiber breakage.
  • the level of foaming can be adjusted much like it is in chemical foaming by altering the injection molding process.
  • the level of gas in the resin is more controlled in technique 1 and is not limited by finding a blowing agent that decomposes at the right temperature for a given process.
  • the process is limited by the short distance within the barrel where the gas is introduced and has to be homogenized with the melt. By consequence the amount of shear applied over this distance is high.
  • a type of mixing element is used which can apply a high shear load to the melt, thereby causing glass fiber breakage.
  • the average fiber length can be reduced by 25%, for example, 30%, for example, 40% as compared to similarly dimensioned solid parts.
  • the surface of the part will show a lot of splay due to gas in the resin being smeared between the resin and the surface of the mold.
  • the amount of splay will depend on the level of gas and the level of weight reduction and to some degree the resin being foamed.
  • the plasticizing unit of the injection molding machine can be pressurized with a gaseous blowing agent.
  • a seal can be installed between the screw shaft and the plasticizing cylinder.
  • the plasticizing unit can be sealed with an airlock that is mounted between the barrel and the material hopper. Similar to other foaming processes, the plasticizing unit can be equipped with a shut-off nozzle and a position control for the screw to keep the blowing-agent-loaded melt under pressure until it is injected into the mold.
  • the fiber length of the long glass fibers in the foamed part after molding can be greater than or equal to the fiber length of long glass fibers in solid molding.
  • the fiber length can be increased 5% to 40% as compared to a non-foamed part.
  • the fiber length can be increased greater than or equal to 5%.
  • the fiber length can be increased greater than or equal to 10%.
  • the fiber length can be increased greater than or equal to 20%.
  • the fiber length can be increased greater than or equal to 25%.
  • the fiber length can be increased greater than or equal to 30%.
  • the fiber length can be increased greater than or equal to 40%.
  • Desirable processing conditions can be achieved when an increase in gas pressure is accompanied by an increase of the back pressure, with a difference between the two of greater than or equal to ⁇ 1 to 10 megaPascals (MPa).
  • the difference can be 0 to 7 MPa.
  • the difference can be 0 to 5 MPa.
  • the difference can be 0 to 0.5 MPa.
  • the difference can be 0.1 to 0.4 MPa.
  • the blowing agent pressure can be 0.1 to 10 MPa, for example, 0.5 to 7.5 MPa, for example 0.75 to 6 MPa, for example 1.5 to 5 MPa, for example, 2.0 to 4.0 MPa.
  • the injection pressure of the injection molding machine can be reduced by greater than or equal to 10% less in making the foamed part including long glass fibers as compared to the injection pressured used to make a similarly dimensioned non-foamed part including long glass fibers.
  • the injection pressure can be reduced by greater than or equal to 20%, for example, greater than or equal to 30% less, for example, greater than or equal to 40% less.
  • a difference between back pressure and the blowing agent pressure of the injection molding machine can be 0 to 10 MPa, for example, 0 to 5 MPa, for example, 0 to 2.5 MPa.
  • the plasticizing unit can be pressurized with any blowing agent that is gaseous at room temperature up to the pressure where the blowing agent liquefies.
  • the equipment can be used with blowing agent pressures of greater than or equal to 7.5 MPa, for example, greater than or equal to 10 MPa, for example, greater than or equal to 15 MPa, for example, greater than or equal to 20 MPa.
  • the gaseous blowing agent diffuses into the polymer pellets in the plasticizing unit.
  • the time required for saturation of the polymer decreases by increasing the temperature due to the higher diffusion rate at higher temperatures. Therefore, the diffusion in the plasticizing unit is fast enough to allow a continuous injection molding production with cycle times of less than or equal to 40 seconds for preloading the polymer with gas.
  • the cycle time can be less than or equal to 35 seconds.
  • the cycle time can be less than or equal to 30 seconds.
  • the cycle time can be less than or equal to 25 seconds.
  • the blowing agent is dissolved in the molten polymer. As a result, no additional mixing elements which might damage the polymeric material or the glass fibers due to additional shear are necessary.
  • Blowing agents for this process can include carbon dioxide and nitrogen at pressures of 0.5 to 5.0 MPa, for example greater than or equal to 5.0 MPa. Since the foaming process can be controlled by only two additional process parameters, i.e., type of blowing agent and pressure, the methods disclosed herein for forming a foamed polymer part using long glass fiber filled polymeric material can be accomplished as easily as with chemical blowing agents.
  • Possible polymeric resins that may be employed include, but are not limited to, oligomers, polymers, ionomers, dendrimers, copolymers such as graft copolymers, block copolymers (e.g., star block copolymers, random copolymers, etc.) and combinations comprising at least one of the foregoing.
  • polymeric resins include, but are not limited to, polycarbonates (e.g., blends of polycarbonate (such as, polycarbonate-polybutadiene blends, copolyester polycarbonates)), polystyrenes (e.g., copolymers of polycarbonate and styrene, polyphenylene ether-polystyrene blends), polyimides (e.g., polyetherimides), acrylonitrile-styrene-butadiene (ABS), polyalkylmethacrylates (e.g., polymethylmethacrylates), polyesters (e.g., copolyesters, polythioesters), polyolefins (e.g., polypropylenes and polyethylenes, high density polyethylenes, low density polyethylenes, linear low density polyethylenes), polyamides (e.g., polyamideimides), polyarylates, polysulfones (e.g., polyarylsulf
  • the polymeric can include, but is not limited to, polycarbonate resins (e.g., LEXANTM resins, commercially available from SABIC's Innovative Plastics business such as LEXANTM XHT, LEXANTM HFD, etc.), polyphenylene ether-polystyrene blends (e.g., NORYLTM resins, commercially available from SABIC's Innovative Plastics business), polyetherimide resins (e.g., ULTEMTM resins, commercially available from SABIC's innovative Plastics business), polybutylene terephthalate-polycarbonate blends (e.g., XENOYTM resins, commercially available from SABIC's innovative Plastics business), copolyestercarbonate resins (e.g.
  • polycarbonate resins e.g., LEXANTM resins, commercially available from SABIC's Innovative Plastics business such as LEXANTM XHT, LEXANTM HFD, etc.
  • LEXANTM SLX or LEXANTM FST resins commercially available from SABIC's Innovative Plastics business
  • acrylonitrile butadiene styrene resins e.g., CYCOLOYTM resins, commercially available from SABIC's Innovative Plastics business
  • polyetherimide/siloxane resins e.g., SILTEMTM, commercially available from SABIC's Innovative Plastics business
  • polypropylene resins for example, long glass fiber filled polypropylene resins (e.g., STAMAXTM resins, commercially available from SABIC's innovative Plastics business), and combinations comprising at least one of the foregoing resins.
  • the polymeric resins can include, but are not limited to, homopolymers and copolymers of a polycarbonate, a polyester, a polyacrylate, a polyamide, a polyetherimide, a polyphenylene ether, or a combination comprising at least one of the foregoing resins.
  • the polycarbonate can comprise copolymers of polycarbonate (e.g., polycarbonate-polysiloxane, such as polycarbonate-polysiloxane block copolymer), linear polycarbonate, branched polycarbonate, end-capped polycarbonate (e.g., nitrile end-capped polycarbonate) blends of PC, such as PC/ABS blend, and combinations comprising at least one of the foregoing, for example a combination of branched and linear polycarbonate.
  • polycarbonate e.g., polycarbonate-polysiloxane, such as polycarbonate-polysiloxane block copolymer
  • linear polycarbonate e.g., polycarbonate-polysiloxane, such as polycarbonate-polysiloxane block copolymer
  • branched polycarbonate branched polycarbonate
  • end-capped polycarbonate e.g., nitrile end-capped polycarbonate
  • the polymeric material can also comprise blowing agent(s).
  • the blowing agent(s) can be of the decomposition type (evolves a gas (e.g., carbon dioxide (CO 2 ), nitrogen (N 2 ), and/or ammonia gas) upon chemical decomposition), and/or an evaporation type (which vaporizes without chemical reaction).
  • blowing agents include, carbon dioxide, sodium bicarbonate, azide compounds, ammonium carbonate, ammonium nitrite, monosodium citrate, light metals which evolve hydrogen upon reaction with water, chlorinated hydrocarbons, chlorofluorocarbons, azodicarbonamide, N,N′dinitrosopentamethylenetetramine, trichloromonofluoromethane, trichlorotrifluoroethane, methylene chloride, organic carboxylic acids (such as formic acid, acetic acid, oxalic acid, ricinoleic acid, and so forth), pentane, butane, ethanol, acetone, nitrogen gas (N 2 ), ammonia gas, and so forth, as well as combinations comprising at least one of the foregoing.
  • organic carboxylic acids such as formic acid, acetic acid, oxalic acid, ricinoleic acid, and so forth
  • pentane butane
  • ethanol acetone
  • Exemplary commercial blowing agents useful for extrusion and molding include, but are not limited to, 6257 ID Endo Foam 35 XFC, 5767 ID Endo Foam 100FC, 8812 ID Exo Foam 80, 8861 ID 25, 6851 ID 35 MFC, 6400 ID 35 NA, 6295 ID 70 XFC, 6265 ID 70 MFC, 7800 ID 70 NA, 6905 ID 90 NA, 6906 ID 90 NA FC, 6258 ID 100 XFC 100, 6836 ID 130 MFC, 6950 ID 40 EEFC, 6952 ID 40 EEXFC, 6112 ID 70 EEFC, 6833 ID 70 EEFC, 8085 ID 70 EEMFC, 7236 ID Foam EEFC, 7284 ID 80 2300 EXO, 7285 OD 80 2400 EXO, 71531 ID 100 MFC EXO, 8016 ID 120 EXO, 6831 ID 135 EXO, Palmarole EXP 141/92B, Palmarole BA.K2.S
  • the blowing agent can be at least one from carbon dioxide, sodium bicarbonate, azide compounds, ammonium carbonate, ammonium nitrite, monosodium citrate, light metals which evolve hydrogen upon reaction with water, chlorinated hydrocarbons, chlorofluorocarbons, azodicarbonamide, N,N′dinitrosopentamethylenetetramine, trichloromonofluoromethane, trichlorotrifluoroethane, methylene chloride, organic carboxylic acids (such as formic acid, acetic acid, oxalic acid, ricinoleic acid, and so forth), pentane, butane, ethanol, acetone, oxygen gas, nitrogen gas, ammonia gas, and combinations comprising at least one of the foregoing.
  • organic carboxylic acids such as formic acid, acetic acid, oxalic acid, ricinoleic acid, and so forth
  • pentane butane, ethanol, acetone, oxygen
  • the cells can be open or closed, but generally are closed.
  • the cells can have an aspect ratio of less than or equal to 10, specifically, less than or equal to 7.5, more specifically, less than or equal to 5, even more specifically, less than or equal to 3.
  • the cells can have a size of less than or equal to 5 millimeters (mm), for example, less than or equal to 2.5 mm, for example, less than or equal to 1 mm, for example, less than or equal to 500 micrometers ( ⁇ m).
  • the cell size can be less than or equal to 250 micrometers, for example, less than or equal to 200 micrometers, for example, less than or equal to 100 micrometers, for example, less than or equal to 50 micrometers, and for example, less than or equal to 20 micrometers.
  • the amount of chemical blowing agent employed is dependent upon the process, processing conditions, and the specific polymeric material(s).
  • the amount of blowing agent can be 0.1 wt. % to 10 wt. %, or, for example, 0.1 wt. % to 5 wt. %, or, for example, 1 wt. % to 4 wt. %, wherein the weight percent is based upon a total weight of the polymer composition (e.g., polymeric material(s), additive(s), blowing agent(s), nucleating agent(s), etc.)
  • the blowing agent can be 0.1 wt. % to 4 wt. %, or, for example, 0.5 wt. % to 3 wt. %, and 0.25 wt. % to 2 wt.
  • blowing agent(s) 0.5 wt. % to 1.5 wt. % of the additional blowing agent(s).
  • additional blowing agent(s) encompass CO 2 , N 2 , H 2 O, O 2 , acetone, butane, and argon.
  • Ozone depleting agents can be avoided due to environmental concerns.
  • resin additive package will be based upon the blowing agent.
  • an additive package will be included so as to counteract any counterion produced by the blowing agent. Therefore, an additive can be included in the composition such that the pH can be maintained in a desired range such that when counterions are produced they are neutralized. The desired pH will be dependent upon the particular polymeric material.
  • a buffer can be added to the composition (polymer material) to neutralize counterions produced by the blowing agent.
  • the lightweight sheet performance for long-term physical and mechanical properties including low-and-high temperature cycling performance, elevated temperature performance, resistance to environmental effects such as high humidity, etc., is influenced by resin stability.
  • the resin additive package would be required to provide hydrolytic stability for performance of the chemical and/or physical blowing agent, by-products, and nucleation sites in the same manner as it would prevent premature resin decomposition during, for instance, an aggressive extrusion processing step.
  • sodium bicarbonate thermally decomposes during the polycarbonate melt processing step into sodium carbonate, water and carbon dioxide, of which water and carbon dioxide work as blowing agent gas to form foamed structure in the polycarbonate sheet while the sodium carbonate residue left inside the final polycarbonate foamed sheet is a relatively strong base that can harm hydrothermal resistance of the polycarbonate matrix if the hydrothermal resistance properties or long-term physical and mechanical properties retention is desired.
  • some other chemical blowing agents with neutral or weak acid or weak base nature of their decomposition product residue at the temperature of the foaming process, may be friendlier to polycarbonate.
  • the examples include mono-sodium citrate, citric acid, 5-phenyl-3,6-dihydro-2H-1,3,4-oxadiazin-2-one (PEDOX), 5-phenyl-1H-Tetrazole (5-PT), as well as combinations comprising at least one of these chemical blowing agents.
  • the polymeric material includes long glass fibers.
  • Long glass fibers as described herein, include glass fibers with an initial length of greater than or equal to 3 mm.
  • the polymeric can include various additives ordinarily incorporated into polymer compositions of this type, with the proviso that the additive(s) are selected so as to not significantly adversely affect the desired properties of the foamed part, in particular, mechanical properties, such as impact resistance.
  • Such additives can be mixed at a suitable time during the mixing of the polymeric material for the foamed part.
  • Exemplary additives include impact modifiers, fillers, reinforcing agents, antioxidants, heat stabilizers, light stabilizers, ultraviolet (UV) light stabilizers, plasticizers, lubricants, mold release agents, antistatic agents, colorants (such as carbon black and organic dyes), surface effect additives, anti-ozonants, thermal stabilizers, anti-corrosion additives, flow promoters, pigments, dyes radiation stabilizers (e.g., infrared absorbing), flame retardants, and anti-drip agents.
  • a combination of additives can be used, for example a combination of a heat stabilizer, mold release agent, and ultraviolet light stabilizer.
  • the additives are used in the amounts generally known to be effective.
  • the total amount of additives is generally 0.001 wt % to 5 wt %, based on the total weight of the polymeric material composition.
  • a method of making a foamed part can include introducing a long glass fiber filled polymeric material to a hopper of an injection molding machine, where the long glass fibers can have an initial, pre-molding length. The long glass fiber filled polymeric material can then be melted.
  • a plasticizing unit of an injection molding machine can then be pressurized with a blowing agent, where a seal can be located between a rotating part and a fixed part of the plasticizing unit. The plasticizing unit can then be sealed with an airlock mounted between a barrel of the injection molding machine to homogenize the melt and the blowing agent. The foamed part can then be formed.
  • a post-molding length of the long glass fibers in the foamed part can be greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned foamed part made by injection molding without the pressurized plasticizing unit.
  • the post-molding length of the long glass fibers can be greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned solid (i.e., non-foamed) part.
  • a weight of the foamed part can be reduced by greater than or equal to 5% as compared to a similarly dimensioned non-foamed part including long glass fibers.
  • the weight reduction can be greater than or equal to 10%.
  • the weight reduction can be greater than or equal to 20%.
  • the weight reduction can be greater than or equal to 30%.
  • Thickness shrinkage of the foamed part can also be reduced when processed via the method disclosed herein with the pressurized unit on the injection molding machine. For example, for a foamed injected plaque with a nominal thickness e.g., 3 mm, a foamed part can have almost 50% less thickness shrinkage than a solid part.
  • a foamed part can have a thickness of 2.92 mm, while a solid part can have a thickness of 2.85 mm.
  • the foamed part in this instance has nearly 50% less thickness shrinkage than the solid part.
  • a foamed injected plaque with a nominal thickness made using the process disclosed herein can have 5% less thickness shrinkage, for example 10% less thickness shrinkage, for example 25% less thickness shrinkage, for example 30% less thickness shrinkage, for example, 50% less thickness shrinkage, for example, 65% less thickness shrinkage as compared to a non-foamed injected plaque.
  • Formed articles include, for example, computer and business machine housings, home appliances, trays, plates, handles, helmets, automotive parts such as instrument panels, cup holders, glove boxes, interior coverings and the like.
  • formed articles include, but are not limited to, food service items, medical devices, animal cages, electrical connectors, enclosures for electrical equipment, electric motor parts, power distribution equipment, communication equipment, computers and the like, including devices that have molded in snap fit connectors.
  • articles of the present invention comprise exterior body panels and parts for outdoor vehicles and devices including automobiles, protected graphics such as signs, outdoor enclosures such as telecommunication and electrical connection boxes, and construction applications such as roof sections, wall panels and glazing.
  • Multilayer articles made of the disclosed polycarbonates particularly include articles which will be exposed to UV-light, whether natural or artificial, during their lifetimes, and most particularly outdoor articles; i.e., those intended for outdoor use.
  • Suitable articles are exemplified by enclosures, housings, panels, and parts for outdoor vehicles and devices; enclosures for electrical and telecommunication devices; outdoor furniture; aircraft components; boats and marine equipment, including trim, enclosures, and housings; outboard motor housings; depth finder housings, personal water-craft; jet-skis; pools; spas; hot-tubs; steps; step coverings; building and construction applications such as glazing, roofs, windows, floors, decorative window furnishings or treatments; treated glass covers for pictures, paintings, posters, and like display items; wall panels, and doors; protected graphics; outdoor and indoor signs; enclosures, housings, panels, and parts for automatic teller machines (ATM); enclosures, housings, panels, and parts for lawn and garden tractors, lawn mowers, and tools, including lawn and garden tools; window and door trim; sports equipment and
  • the foamed parts can include articles comprising the disclosed long glass fiber filled polymeric materials.
  • the article comprising the disclosed long glass fiber filled polymeric materials can be used in automotive applications.
  • the article comprising the disclosed long glass fiber filled polymeric materials can be selected from instrument panels, overhead consoles, interior trim, center consoles, panels, quarter panels, rocker panels, trim, fenders, doors, deck lids, trunk lids, hoods, bonnets, roofs, bumpers, fascia, grilles, minor housings, pillar appliqus, cladding, body side moldings, wheel covers, hubcaps, door handles, spoilers, window frames, headlamp bezels, headlamps, tail lamps, tail lamp housings, tail lamp bezels, license plate enclosures, roof racks, and running boards.
  • the article comprising the disclosed long glass fiber filled polymeric materials can be selected from mobile device exteriors, mobile device covers, enclosures for electrical and electronic assemblies, protective headgear, buffer edging for furniture and joinery panels, luggage and protective carrying cases, small kitchen appliances, and toys.
  • the foamed parts can include electrical or electronic devices including the disclosed long glass fiber filled polymeric materials.
  • the electrical or electronic device can be a cellphone, a MP3 player, a computer, a laptop, a camera, a video recorder, an electronic tablet, a pager, a hand receiver, a video game, a calculator, a wireless car entry device, an automotive part, a filter housing, a luggage cart, an office chair, a kitchen appliance, an electrical housing, an electrical connector, a lighting fixture, a light emitting diode, an electrical part, or a telecommunications part.
  • the methods disclosed herein can provide favorable results with respect to the use of long glass fiber filled materials since the loss of mechanical properties due to foaming is less compared with other foaming technologies (such as chemical and those foamed with MuCellTM technology) and fiber length is upheld or increased as compared to the original fiber length in solid moldings. Furthermore, initial cost for adapting the injection unit is low as only the pressurizing unit is an additional component.
  • Weight reduction of the foamed parts can be less than or equal to 65%, for example, less than or equal to 50%, for example, less than or equal to 30%, for example, less than or equal to 25%, for example, less than or equal to 20%, for example, less than or equal to 15%, for example, less than or equal to 10%, for example, less than or equal to 5% as compared to a solid (i.e., non-foamed part) part with the same thickness.
  • a weight reduction of less than or equal to 20% can also provide the desired impact properties.
  • compositions 1 to 5 included a long glass fiber filled polypropylene polymeric material commercially available from SABIC's innovative Plastics business.
  • Composition 6 included a short glass fiber filled polypropylene compound (PPC) commercially available from SABIC's Innovative Plastics business. Microanalysis was used to evaluate gas distribution within the foamed samples. Samples were cut to size with the use of a band saw. For cross-sectional images, samples were embedded in epoxy resin. All samples were polished with a polishing machine and images were done with light microscopy. For density measurements, dimensions were measured with a caliper an weighed on an analytical balance. “YM” in the material description refers to a polypropylene monomer, while “YK” in the material description refers to a polypropylene copolymer.
  • PPC polypropylene compound
  • Weight reduction of the foamed parts Example Nos. 1-4, and 1-5, having a thickness of 3 mm as compared to reference parts, Example Nos. 1-1, 1-2, and 1-3, having the same thickness, was nearly 30% for all different grades of STAMAXTM used as can be seen in Table 2. Using the process disclosed herein, weight reduction can be achieved without any additional processing requirements, such as injection decompression.
  • FIGS. 1A to 1F illustrate cut sections of a foamed plaque of Example 1-4 having a 30% weight reduction as compared to the same size solid part, Example 1-1.
  • the foamed cells in the final part were well distributed as can be seen in FIG. 1 .
  • Cross and in-flow sections for Example 1-5 showed a weight reduction of greater than 20%.
  • the surface layer was well defined closer to the gate, but thicker to the end. The cell structure appears to be similar in all sections.
  • FIGS. 2A to 2F illustrate cut sections of a foamed plaque of Example 1-5 having a 20% weight reduction as compared to the same size solid part, Example 1-2.
  • FIGS. 3A to 3C illustrate the positions on the samples where the measurements (including samples for microscopy analysis) were taken, where the gate is indicated by reference number 10 and the direction of flow is indicated by arrow 12 .
  • FIGS. 4A, 4B , and FIGS. 5A to 5D are displayed in FIGS. 4A, 4B , and FIGS. 5A to 5D , where FIGS. 4A and 4B illustrate the positions where the measurements were taken.
  • FIGS. 5A to 5D the cell structure is much more irregular with some large gap openings due to decompression (i.e., opening of the tool). Nevertheless the entire structure seems still relatively stable and if eventual improvement of the melt strength of the polymer can be achieved, it is believed that the structure could be quite uniform.
  • FIGS. 6A and 6B Cross and in-flow sections for plaques molded with STAMAXTM 30YK270E, i.e., Example 2-2 and decompression to 4 times original thickness are displayed in FIGS. 6A and 6B .
  • cell structure is not consistent and clear separation of the layers is observed in the middle of the sample.
  • the polymer bonds are not present in the middle of the part and only the glass fibers establishing connection between the two separated layers. This indicates that increase of the thickness by decompression greater than 2 to 2.5 times the original thickness is not applicable for applications with high mechanical requirements, but could be a useful technology for applications with sound and insulation requirements.
  • the core contains polymer resin, glass fibers and voids.
  • the shell contains only polymer resin and glass fibers.
  • the shell thickness can vary from 0.2 mm to 0.5 mm, for this particular thickness. The shell becomes thicker when further away from the gate.
  • injection pressure could be reduced by 10 to 20%. It was further discovered that the gas pressure has an influence on the foaming of the part. For example, increase of gas pressure has to be accompanied by the increase of the back pressure as well, because the gas pressure acts like a contra pressure against back pressure and if back pressure is under the pressure of the gas, then plasticizing is difficult. In these examples, a gap of 0.5 MPa was left between the gas pressure and the back pressure. With the use of higher gas pressure and back pressure respectively as well, the weight reduction in the part was better. It was observed that change of the gas pressure from 3.5 MPa to 5.0 MPa yields an additional 2.5% weight reduction. However, a negative impact on the fiber length was observed.
  • the packing time i.e., the time after injection when opening of the mold is occurring, has an important role in determining the thickness of the surface layer of the molded part and also the overall mechanical performance. This time cannot be too long, because the inner layer still has to be melted, when opening occurs to allow the gas to expand. Thickness of the part is a main factor in determining this time. For the particular parts used in this study, the time was 5 seconds.
  • Fiber length is a parameter of interest in the mechanical performance of long glass fiber filled materials. Measurement of the fiber length was performed on the purge for all foamed conditions and for conditions without foaming as a reference point. Apart from the purge, for all samples, measurement was done at the end of the flow path at 20 mm of the far end of the plaque and for most of the samples fiber measurement was done also at a position after the gate, i.e., 20 mm after the gate.
  • FIG. 7 Measured fiber length in the specimens collected at 20 mm from the far end of the plaque with solid STAMAXTM material 2 and with foamed STAMAXTM material 4 is illustrated in FIG. 7 .
  • Examples 4-1 and 4-6 were made from Composition No. 1 with Example 4-1 being solid and Example 4-6 being foamed.
  • Examples 4-2 and 4-7 were made from Composition No. 2 with Example 4-2 being solid and Example 4-7 being foamed.
  • Examples 4-3 and 4-8 were made from Composition No. 3 with Example 4-3 being solid and Example 4-8 being foamed.
  • Examples 4-4 and 4-9 were made from Composition No. 4 with Example 4-4 being solid and Example 4-9 being foamed, and Examples 4-5 and 4-10 were made from Composition No.
  • Example 5 with Example 4-5 being solid and Example 4-10 being foamed.
  • the glass fiber length in the foamed samples is clearly longer than solid samples. This indicates that by applying a pressurized unit during foaming injection molding, the glass fiber length is not only maintained as the glass fiber length for solid material, but actually an increase of the fiber length can be present.
  • FIG. 8 illustrates that for Examples 4-1 (solid) and 4-2 (foamed), the quantity of long glass fibers, i.e., greater than or equal to 6 mm, are greater in the foamed part.
  • FIG. 11 illustrates fiber length measurements in the purge with foaming for the method disclosed herein and the MuCellTM method.
  • Samples 11-1 and 11-2 were made from Composition 1 in Table 1
  • Samples 11-3 and 11-4 were made from Composition 2in Table 1
  • Samples 11-5 and 11-6 were made from Composition 3 in Table 1
  • Samples 11-7 and 11-8 were made from Composition 4 in Table 1
  • Samples 11-9 and 11-10 were made from Composition 5 in Table 1.
  • Samples 11-1, 11-3, 11-5, 11-7, and 11-9 were made using the method disclosed herein (reference number 14 )
  • Samples 11-2, 11-4, 11-6, 11-8, and 11-10 were made using the MuCellTM method (reference number 16 ).
  • fiber length in the purge after foaming are greater for each composition tested with the method disclosed herein.
  • Ash content was measured in the solid parts and in foamed parts as well.
  • Examples 5-1 and 5-3 were made from Composition 1, where Example 5-1 was solid and Example 5-3 was foamed.
  • Examples 5-2 and 5-4 were made from Composition No. 2, where Example 5-3 was solid and Example 5-4 was foamed. Measurement was done in three locations plus one location in the sprue, and the results are illustrated in FIG. 9 where flow length measured in mm is indicated horizontally and ash content in percent is indicated vertically. The first measurement is in the sprue and is indicated as ⁇ 10 mm. The 0 point is assumed to be the gate of the part.
  • the ash content at the end of the fill is higher for foamed plaques than solid ones. This can be associated with transport of longer fibers present in foamed parts at the end of the flow.
  • FIG. 10 Results for density distribution along a flow path for the MuCellTM technology and the method disclosed herein are illustrated in FIG. 10 where density measured in g/cm 3 is plotted versus flow length measured in mm.
  • Samples 10-1 and 10-2 were made from the same grade of polypropylene having Composition 5 listed in Table 1, while Samples 10-3 and 10-4 were made from the sample grade of polypropylene having Composition 2 listed in Table 1.
  • Samples 10-1 and 10-3 were processed according to the method disclosed herein with an injection rate of 45 cubic centimeters per second (cm 3 /s), while Samples 10-2 and 10-4 were processed according to the MuCellTM method with an injection rate of 100 cm 3 /s.
  • FIG. 10 results for density distribution along a flow path for the MuCellTM technology and the method disclosed herein are illustrated in FIG. 10 where density measured in g/cm 3 is plotted versus flow length measured in mm.
  • Samples 10-1 and 10-2 were made from the same grade of polypropylene having Com
  • Samples 10-1 and 10-3 demonstrate uniform density distribution with a negligible difference between the beginning and end of the flow. Conversely, Samples 10-2 and 10-4 demonstrate a difference of up to 10%, which is even starker when taking into consideration that the injection rate for Samples 10-2 and 10-4 was over double that of Samples 10-1 and 10-3. Density distribution can have an influence on the properties and final performance of any articles molded.
  • FIGS. 12A to 12D illustrate the results where isotropic flexural strength was observed to be higher for samples processed according to the method disclosed herein as compared to samples processed according to the MuCellTM method.
  • Samples 12A1-4 were made from Composition 1 in Table 1
  • Samples 12B1-B4 were made from Composition 2 in Table 1
  • Samples 12C1-4 were made from Composition 4 in Table 1
  • Samples 12D1-4 were made from Composition 5 in Table 1.
  • Samples 12A1-2, 12B1-2, 12C1-2, and 12D1-2 were not foamed, while Samples 12A3-4, 12B3-4, 12C3-4, and 12D3-4 were foamed with a 20% weight reduction.
  • Samples 12A1, 12A3, 12B1, 12B3, 12C1, 12C3, 12D1, and 12D3 were made according to the method disclosed herein, while Samples 12A2, 12A4, 12B2, 12B4, 12C2, 12C4, 12D2, and 12D4 were made according to the MuCellTM method.
  • Samples 12A3, 12A4, 12B3, 12B4, 12C3, 12C4, 12D3, and 12D4 each had a 20% weight reduction as compared to the solid samples.
  • flexural strength is higher for the samples produced according to the method disclosed herein.
  • flexural properties are higher with the method disclosed herein for the foamed samples than for the foamed samples made according to the MuCellTM method.
  • Samples 13A1-13A6 were made from Composition 1 in Table 2, while Samples 13B1-13B2 were made from Composition 5 in Table 1. Samples 13A1, 13A2, 13B1, and 13B2 were made without foaming; Samples 13A3, 13A4, 13B3, and 13B4 were made by foaming with a 20% weight reduction where Samples 13A3 and 13B3 were made according to the method disclosed herein and Samples 13A4 and 13B4 were made according to the MuCellTM method; Samples 13A5, 13A6, 13B5, and 13B6 were made by foaming with a 30% weight reduction, wherein Samples 13A5 and 13B5 were made according to the method disclosed herein and Samples 13A6 and 13B6 were made according to the MuCellTM method.
  • FIGS. 13A and 13B Penetration energy at 17 mm displacement measured in Joules per millimeter (J/mm) was measured and is plotted in FIGS. 13A and 13B .
  • impact properties are higher for the samples processed with the method disclosed herein as compared to the samples processed with the MuCellTM method. Additionally, reduction of the penetration energy for Samples 13A3, 13A4, 13B3, and 13B4 is lower for samples 13A3 and 13B4, both processed with the method disclosed herein likely due to the longer fibers in each part.
  • FIGS. 14A and 14B Impact properties for decompression molded samples were also tested according to ISO 6603-2:2000 (A3). Results are illustrated in FIGS. 14A and 14B , where, all of the samples were made with Composition 2. Samples 14A1, 14A2, 14B1, and 14B2 were made without foaming, while Samples 14A3, 14A4, 14B3, and 14B4 were foamed with a thickness 2.3 times the thickness of the solid part. Samples 14A1, 14A3, 14B1, and 14B3 were made according to the method disclosed herein, while Samples 14A2, 14A4, 14B2, 14B4 were made according to the were made according to the MuCellTM method. FIG. 14A illustrates penetration energy at a displacement of 17 mm measured in Jimm and FIG.
  • FIG. 14B illustrates the maximum force measured in Newtons (N).
  • N the maximum force measured in Newtons
  • Embodiment 1 A method of making a foamed part, comprising: introducing a long glass fiber filled polymeric material to a hopper of an injection molding machine, wherein the long glass fibers have a pre-molding length; melting the long glass fiber filled polymeric material to form a melt; pressurizing a plasticizing unit of the injection molding machine with a blowing agent, wherein a seal is located between a rotating part and a fixed part of the plasticizing unit; having a seal between rotating and fixed part of the plasticizing unit; sealing the plasticizing unit with an airlock mounted between a barrel of the injection molding machine and the hopper; increasing a pressure of the blowing agent and increasing a back pressure of the injection molding machine to homogenize the melt and the blowing agent; and forming the foamed part; wherein a post-molding length of the long glass fibers in the foamed part is greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned foamed part made without the pressurized
  • Embodiment 2 The method of Embodiment 1, wherein the post-molding length of the long glass fibers in the foamed part is greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned non-foamed part.
  • Embodiment 3 The method of Embodiment 1 or Embodiment 2, wherein the blowing agent is a gaseous blowing agent.
  • Embodiment 4 The method of Embodiment 3, wherein the blowing agent is at least one from carbon dioxide, sodium bicarbonate, azide compounds, ammonium carbonate, ammonium nitrite, monosodium citrate, light metals which evolve hydrogen upon reaction with water, chlorinated hydrocarbons, chlorofluorocarbons, azodicarbonamide, N,N′dinitrosopentamethylenetetramine, trichloromonofluoromethane, trichlorotrifluoroethane, methylene chloride, organic carboxylic acids (such as formic acid, acetic acid, oxalic acid, ricinoleic acid, and so forth), pentane, butane, ethanol, acetone, oxygen gas, nitrogen gas, ammonia gas, and combinations comprising at least one of the foregoing.
  • the blowing agent is at least one from carbon dioxide, sodium bicarbonate, azide compounds, ammonium carbonate, ammonium nitrite, monoso
  • Embodiment 5 The method of Embodiment 4, wherein the blowing agent is at least one from nitrogen gas, oxygen gas, carbon dioxide gas, and a combination comprising at least one of the foregoing.
  • Embodiment 6 The method of any of Embodiments 1-5, wherein a weight of the foamed part is reduced by greater than or equal to 5% as compared to a similarly dimensioned non-foamed part including long glass fibers.
  • Embodiment 7 The method of any of Embodiments 1-6, wherein a foamed injected plaque has 10% less thickness shrinkage as compared to a non-foamed injected plaque.
  • Embodiment 8 The method of any of Embodiments 1-7, wherein a foamed injected plaque has 50% less thickness shrinkage as compared to non-foamed injected plaque.
  • Embodiment 9 The method any of Embodiments 1-8, wherein the blowing agent pressure and the back pressure of the injection molding machine differ by greater than or equal to 0 megaPascals.
  • Embodiment 10 The method of any of Embodiments 1-9, wherein the blowing agent pressure or the back pressure of the injection molding machine is 0 to 10 megaPascals.
  • Embodiment 11 The method of any of Embodiments 1-10, wherein the difference between back pressure and the blowing agent pressure of the injection molding machine is 0 to 5 megaPascals.
  • Embodiment 12 The method of any of Embodiments 1-11, wherein the polymeric material is at least one from polycarbonate, polypropylene, polyarylate, polyester, polyphenylene ether, polystyrene, acrylonitrile butadiene styrene, polyether, polyimide, polyetherimide, polysulfone, polyether ketone, polyether ether ketone, poly(methyl methacrylate), polyvinyl chloride, polysiloxane, and combinations comprising at least one of the foregoing.
  • the polymeric material is at least one from polycarbonate, polypropylene, polyarylate, polyester, polyphenylene ether, polystyrene, acrylonitrile butadiene styrene, polyether, polyimide, polyetherimide, polysulfone, polyether ketone, polyether ether ketone, poly(methyl methacrylate), polyvinyl chloride, polysiloxane, and combinations comprising
  • Embodiment 13 The method of any of Embodiments 1-12, wherein an injection pressure of the injection molding machine is greater than or equal to 10% less in making the foamed part as compared to the injection pressure when making a non-foamed part including long glass fibers.
  • Embodiment 14 A polymeric part made by the method of any of Embodiments 1-13.
  • Embodiment 15 A foamed part, comprising: a long glass fiber filled polymeric material, wherein the long glass fibers have an initial length before molding of the foamed part and a final length after molding of the foamed part; wherein a post-molding length of the long glass fibers in the foamed part is greater than or equal to a post-molding length of long glass fibers in a similarly dimensioned foamed part made without a pressurized plasticizing unit.
  • Embodiment 16 The foamed part of Embodiment 15, wherein the polymeric material is at least one from polycarbonate, polypropylene, polyarylate, polyester, polyphenylene ether, polystyrene, acrylonitrile butadiene styrene, polyether, polyimide, polyetherimide, polysulfone, polyether ketone, polyether ether ketone, poly(methyl methacrylate), polyvinyl chloride, polysiloxane, and combinations comprising at least one of the foregoing.
  • the polymeric material is at least one from polycarbonate, polypropylene, polyarylate, polyester, polyphenylene ether, polystyrene, acrylonitrile butadiene styrene, polyether, polyimide, polyetherimide, polysulfone, polyether ketone, polyether ether ketone, poly(methyl methacrylate), polyvinyl chloride, polysiloxane, and combinations comprising at
  • Embodiment 17 The foamed part of Embodiment 15 or Embodiment 16, wherein the final length of the long glass fibers in the foamed part is increased as compared to a similarly dimensioned non-foamed part including long glass fibers.
  • Embodiment 18 The foamed part of any of Embodiments 15-17, wherein a weight of the foamed part is reduced by greater than or equal to 5% as compared to a similarly dimensioned non-foamed part including long glass fibers.
  • Embodiment 19 The foamed part of any of Embodiments 15-18, wherein a foamed injected plaque has 10% less thickness shrinkage as compared to a non-foamed injected plaque.
  • Embodiment 20 The foamed part of any of Embodiments 15-19, wherein the foamed part has a number of long glass fibers that is greater than or equal to a number of long glass fibers in a similarly dimensioned non-foamed part including long glass fibers.
  • Embodiment 21 The foamed part of any of Embodiments 15-20, wherein a thickness of the foamed part is increased greater than or equal 50% a thickness of a non-foamed part including long glass fibers.
  • the invention may alternately comprise, consist of, or consist essentially of, any appropriate components herein disclosed.
  • the invention may additionally, or alternatively, be formulated so as to be devoid, or substantially free, of any components, materials, ingredients, adjuvants or species used in the prior art compositions or that are otherwise not necessary to the achievement of the function and/or objectives of the present invention.
  • any reference to standards, regulations, testing methods and the like, such as ISO 6603 and ISO 178 refer to the standard, regulation, guidance or method that is in force at the time of filing of the present application.

Landscapes

  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
US15/304,059 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials Abandoned US20170036378A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US15/304,059 US20170036378A1 (en) 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US201461980228P 2014-04-16 2014-04-16
US15/304,059 US20170036378A1 (en) 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials
PCT/IB2015/052794 WO2015159257A1 (en) 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
PCT/IB2015/052794 A-371-Of-International WO2015159257A1 (en) 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US16/745,505 Division US20200147843A1 (en) 2014-04-16 2020-01-17 Foaming technology in long glass fiber filled materials

Publications (1)

Publication Number Publication Date
US20170036378A1 true US20170036378A1 (en) 2017-02-09

Family

ID=53442812

Family Applications (2)

Application Number Title Priority Date Filing Date
US15/304,059 Abandoned US20170036378A1 (en) 2014-04-16 2015-04-16 Foaming technology in long glass fiber filled materials
US16/745,505 Pending US20200147843A1 (en) 2014-04-16 2020-01-17 Foaming technology in long glass fiber filled materials

Family Applications After (1)

Application Number Title Priority Date Filing Date
US16/745,505 Pending US20200147843A1 (en) 2014-04-16 2020-01-17 Foaming technology in long glass fiber filled materials

Country Status (6)

Country Link
US (2) US20170036378A1 (de)
EP (1) EP3131726B1 (de)
JP (1) JP6721518B2 (de)
KR (1) KR102204791B1 (de)
CN (1) CN106232320B (de)
WO (1) WO2015159257A1 (de)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10233393B2 (en) 2016-07-08 2019-03-19 Golden Renewable Energy, LLC Heated airlock feeder unit
US10345048B2 (en) 2016-05-12 2019-07-09 Golden Renewable Energy, LLC Cyclonic condensing and cooling system
US10436525B2 (en) 2016-05-12 2019-10-08 Golden Renewable Energy, LLC Cyclonic cooling system
US10544367B2 (en) 2016-06-21 2020-01-28 Golden Renewable Energy, LLC Char separator and method
US10633595B2 (en) 2016-06-21 2020-04-28 Golden Renewable Energy, LLC Char separator
WO2021038015A1 (en) * 2019-08-30 2021-03-04 Sabic Global Technologies B.V. Tool part suitable to be used in humid environment
US10961062B2 (en) 2016-06-21 2021-03-30 Golden Renewable Energy, LLC Bag press feeder assembly
US11773330B2 (en) 2016-07-05 2023-10-03 Braven Environmental, Llc System and process for converting waste plastic into fuel

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2017079916A1 (en) * 2015-11-11 2017-05-18 Sabic Global Technologies, B.V. Electrical component carrier as a stressed member of an electrical vehicle
CN105440626B (zh) * 2015-11-28 2018-02-16 惠州卫生职业技术学院 一种阻燃的玻纤聚碳酸酯合金
CN105694257A (zh) * 2016-03-17 2016-06-22 合肥晨煦信息科技有限公司 一种树脂基纤维增强复合材料的制备方法
CN109153161A (zh) * 2016-04-21 2019-01-04 沙特基础工业全球技术公司 使用注射成型发泡工艺与模芯回退工艺结合生产具有提高的冲击性能的零件的方法
CN107096882B (zh) * 2017-06-13 2023-03-21 柳州智云科技有限公司 基于3d打印的铸造用模具及该模具的制备方法
DE102020121179B3 (de) * 2020-08-12 2021-10-14 Pollmann International Gmbh Elektrischer Komponententräger

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0885128A (ja) * 1994-09-19 1996-04-02 Hitachi Ltd 熱可塑性樹脂発泡成形体の製造方法及び装置
JP3697144B2 (ja) * 2000-06-14 2005-09-21 キヤノン株式会社 発泡成形方法及び装置
US7107601B2 (en) * 2000-06-14 2006-09-12 Canon Kabushiki Kaisha Foam molding method and apparatus
AU2001294927A1 (en) * 2000-09-29 2002-04-08 Trexel, Inc. Fiber-filler molded articles
US20030003291A1 (en) * 2001-07-02 2003-01-02 Shah Suresh D. Foamed thermoplastic resin having fiber reinforcing and apparatuses for making
JP2003326571A (ja) * 2002-05-16 2003-11-19 Meiki Co Ltd 可塑化装置と可塑化方法
JP4569417B2 (ja) * 2005-08-23 2010-10-27 宇部興産機械株式会社 熱可塑性樹脂の射出発泡成形方法
JP2007210323A (ja) * 2006-01-10 2007-08-23 Mazda Motor Corp 樹脂成形品の成形方法及び成形装置
JP4748365B2 (ja) * 2006-06-23 2011-08-17 マツダ株式会社 繊維強化樹脂成形品の成形方法及び成形装置
US20090042011A1 (en) 2007-08-10 2009-02-12 Frank Jaarsma Fiber Reinforced Cellular Foam Product
US20130059939A1 (en) * 2010-05-10 2013-03-07 Nitto Boseki Co., Ltd. Method of foam molding of resin reinforced with flat glass fibers
JP5226904B1 (ja) * 2011-08-19 2013-07-03 日立マクセル株式会社 混練装置及び熱可塑性樹脂成形体の製造方法
DE102012001108A1 (de) 2012-01-23 2013-07-25 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren und Vorrichtung zur Herstellung von mit Fasern versetzten Polymerschäumen

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10345048B2 (en) 2016-05-12 2019-07-09 Golden Renewable Energy, LLC Cyclonic condensing and cooling system
US10436525B2 (en) 2016-05-12 2019-10-08 Golden Renewable Energy, LLC Cyclonic cooling system
US10544367B2 (en) 2016-06-21 2020-01-28 Golden Renewable Energy, LLC Char separator and method
US10633595B2 (en) 2016-06-21 2020-04-28 Golden Renewable Energy, LLC Char separator
US10961062B2 (en) 2016-06-21 2021-03-30 Golden Renewable Energy, LLC Bag press feeder assembly
US11542434B2 (en) 2016-06-21 2023-01-03 Golden Renewable Energy, LLC Char separator and method
US11773330B2 (en) 2016-07-05 2023-10-03 Braven Environmental, Llc System and process for converting waste plastic into fuel
US10233393B2 (en) 2016-07-08 2019-03-19 Golden Renewable Energy, LLC Heated airlock feeder unit
WO2021038015A1 (en) * 2019-08-30 2021-03-04 Sabic Global Technologies B.V. Tool part suitable to be used in humid environment

Also Published As

Publication number Publication date
KR102204791B1 (ko) 2021-01-20
EP3131726B1 (de) 2019-11-13
KR20160147824A (ko) 2016-12-23
JP6721518B2 (ja) 2020-07-15
WO2015159257A1 (en) 2015-10-22
US20200147843A1 (en) 2020-05-14
CN106232320A (zh) 2016-12-14
EP3131726A1 (de) 2017-02-22
CN106232320B (zh) 2020-08-04
JP2017513737A (ja) 2017-06-01

Similar Documents

Publication Publication Date Title
US20200147843A1 (en) Foaming technology in long glass fiber filled materials
US20190118434A1 (en) Process for producing parts having increased impact performance by use of an injection molding foaming process in combination with a mold core-back process
Bledzki et al. Injection moulded microcellular wood fibre–polypropylene composites
US6146577A (en) Method for injection molding of thermoplastic resins
US8574473B2 (en) Foamed resin injection molding method
EP3390510B1 (de) Verfahren zur herstellung von formteilen mit ästhetischen oberflächen durch schaumspritzgiessen
US8048347B2 (en) Method of manufacture of a foamed core class “A” article
Bledzki et al. Polycarbonate microfoams with a smooth surface and higher notched impact strength
CN1827340B (zh) 制备热塑性树脂制品的方法
KR101371848B1 (ko) 자동차 내장재용 폴리우레탄 발포조성물
EP3335871B1 (de) Mehrschichtstruktur und daraus hergestellte kraftfahrzeugkomponente
EP3344432B1 (de) Verfahren zur herstellung längerer fasern in spritzgegossenen kompakten bauteilen durch lösen von gas während der plastifizierung
JP2000239437A (ja) ガラス繊維含有膨張成形用材料、膨張成形方法および膨張成形品
JP2000257442A (ja) 自動車エンジンルーム内用軽量樹脂成形品およびその製造方法
KR101269050B1 (ko) 난연성 경량 플라스틱 및 이의 제조방법
Jung Development of innovative gas-assisted foam injection molding technology
JP2007045979A (ja) 自動車用内装材
JP2000255270A (ja) 自動車用サンルーフハウジングまたはサンシェードおよびそれらの製造方法
JP7158600B2 (ja) スペーサー及びその製造方法、並びに複合体
US20230407035A1 (en) Method for producing polyamide-based resin multi-stage-expanded beads
JP2022076286A (ja) 積層体及びその製造方法、並びに防音部材
JP2006094879A (ja) 弾球遊技機の遊技盤
JP2021120189A (ja) 成形体および成形体の製造方法
JP3479386B2 (ja) 長繊維強化プラスチック製窓枠または扉枠
US20120052236A1 (en) Method for producing structural foam and products containing structural foam

Legal Events

Date Code Title Description
AS Assignment

Owner name: SABIC GLOBAL TECHNOLOGIES B.V., NETHERLANDS

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:YANEV, ANGEL;VAES, MARNIK;SCHIJVE, WARDEN;SIGNING DATES FROM 20140414 TO 20140415;REEL/FRAME:040013/0048

STPP Information on status: patent application and granting procedure in general

Free format text: ADVISORY ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: DOCKETED NEW CASE - READY FOR EXAMINATION

STPP Information on status: patent application and granting procedure in general

Free format text: NON FINAL ACTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: RESPONSE TO NON-FINAL OFFICE ACTION ENTERED AND FORWARDED TO EXAMINER

STPP Information on status: patent application and granting procedure in general

Free format text: FINAL REJECTION MAILED

STPP Information on status: patent application and granting procedure in general

Free format text: ADVISORY ACTION MAILED

STCB Information on status: application discontinuation

Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION