EP0554272A1 - Bindersystem und verfahren für die verarbeitung von metallpulver durch spritzgiessen - Google Patents
Bindersystem und verfahren für die verarbeitung von metallpulver durch spritzgiessenInfo
- Publication number
- EP0554272A1 EP0554272A1 EP91917354A EP91917354A EP0554272A1 EP 0554272 A1 EP0554272 A1 EP 0554272A1 EP 91917354 A EP91917354 A EP 91917354A EP 91917354 A EP91917354 A EP 91917354A EP 0554272 A1 EP0554272 A1 EP 0554272A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- binder
- binder system
- metal powder
- polymer component
- component
- 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.)
- Withdrawn
Links
- 239000011230 binding agent Substances 0.000 title claims abstract description 45
- 239000000843 powder Substances 0.000 title claims abstract description 22
- 239000002184 metal Substances 0.000 title claims abstract description 20
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000001746 injection moulding Methods 0.000 title claims abstract description 10
- 230000008569 process Effects 0.000 title abstract description 5
- 229920000642 polymer Polymers 0.000 claims abstract description 15
- 238000005245 sintering Methods 0.000 claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- -1 polyethylene Polymers 0.000 claims description 12
- 239000004743 Polypropylene Substances 0.000 claims description 11
- 229920001155 polypropylene Polymers 0.000 claims description 11
- 239000007789 gas Substances 0.000 claims description 10
- 230000001681 protective effect Effects 0.000 claims description 10
- DDTBPAQBQHZRDW-UHFFFAOYSA-N cyclododecane Chemical compound C1CCCCCCCCCCC1 DDTBPAQBQHZRDW-UHFFFAOYSA-N 0.000 claims description 9
- 150000001875 compounds Chemical class 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- SXVPOSFURRDKBO-UHFFFAOYSA-N Cyclododecanone Chemical compound O=C1CCCCCCCCCCC1 SXVPOSFURRDKBO-UHFFFAOYSA-N 0.000 claims description 4
- 238000000465 moulding Methods 0.000 claims description 4
- GLDOVTGHNKAZLK-UHFFFAOYSA-N octadecan-1-ol Chemical compound CCCCCCCCCCCCCCCCCCO GLDOVTGHNKAZLK-UHFFFAOYSA-N 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- SFVWPXMPRCIVOK-UHFFFAOYSA-N cyclododecanol Chemical compound OC1CCCCCCCCCCC1 SFVWPXMPRCIVOK-UHFFFAOYSA-N 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- GOQYKNQRPGWPLP-UHFFFAOYSA-N n-heptadecyl alcohol Natural products CCCCCCCCCCCCCCCCCO GOQYKNQRPGWPLP-UHFFFAOYSA-N 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 238000010525 oxidative degradation reaction Methods 0.000 claims description 2
- 239000004698 Polyethylene Substances 0.000 claims 1
- 238000002347 injection Methods 0.000 claims 1
- 239000007924 injection Substances 0.000 claims 1
- 229920000573 polyethylene Polymers 0.000 claims 1
- 238000009736 wetting Methods 0.000 abstract description 4
- 239000007787 solid Substances 0.000 abstract description 3
- 239000000243 solution Substances 0.000 abstract description 3
- FZERHIULMFGESH-UHFFFAOYSA-N N-phenylacetamide Chemical compound CC(=O)NC1=CC=CC=C1 FZERHIULMFGESH-UHFFFAOYSA-N 0.000 description 4
- 235000021355 Stearic acid Nutrition 0.000 description 3
- 238000005336 cracking Methods 0.000 description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 3
- 229920000098 polyolefin Polymers 0.000 description 3
- 239000008117 stearic acid Substances 0.000 description 3
- 239000001993 wax Substances 0.000 description 3
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 229960001413 acetanilide Drugs 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- NNBZCPXTIHJBJL-UHFFFAOYSA-N decalin Chemical compound C1CCCC2CCCCC21 NNBZCPXTIHJBJL-UHFFFAOYSA-N 0.000 description 2
- KZTYYGOKRVBIMI-UHFFFAOYSA-N diphenyl sulfone Chemical compound C=1C=CC=CC=1S(=O)(=O)C1=CC=CC=C1 KZTYYGOKRVBIMI-UHFFFAOYSA-N 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000000859 sublimation Methods 0.000 description 2
- 230000008022 sublimation Effects 0.000 description 2
- RLFWWDJHLFCNIJ-UHFFFAOYSA-N Aminoantipyrine Natural products CN1C(C)=C(N)C(=O)N1C1=CC=CC=C1 RLFWWDJHLFCNIJ-UHFFFAOYSA-N 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- VEQOALNAAJBPNY-UHFFFAOYSA-N antipyrine Chemical compound CN1C(C)=CC(=O)N1C1=CC=CC=C1 VEQOALNAAJBPNY-UHFFFAOYSA-N 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- ROORDVPLFPIABK-UHFFFAOYSA-N diphenyl carbonate Chemical compound C=1C=CC=CC=1OC(=O)OC1=CC=CC=C1 ROORDVPLFPIABK-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000001513 hot isostatic pressing Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 229960005222 phenazone Drugs 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000007847 structural defect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- PXXNTAGJWPJAGM-UHFFFAOYSA-N vertaline Natural products C1C2C=3C=C(OC)C(OC)=CC=3OC(C=C3)=CC=C3CCC(=O)OC1CC1N2CCCC1 PXXNTAGJWPJAGM-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F3/00—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces
- B22F3/22—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip
- B22F3/225—Manufacture of workpieces or articles from metallic powder characterised by the manner of compacting or sintering; Apparatus specially adapted therefor ; Presses and furnaces for producing castings from a slip by injection molding
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/08—Metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/01—Hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/05—Alcohols; Metal alcoholates
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/04—Oxygen-containing compounds
- C08K5/07—Aldehydes; Ketones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F2998/00—Supplementary information concerning processes or compositions relating to powder metallurgy
Definitions
- the invention is based on a binder system according to the type of the main claim and a method for processing metal powders into sintered parts using the binder system according to the invention.
- MIM metal injection molding
- Binder systems based on waxes, such as paraffin wax, are known, e.g. B. from the lecture by Chan I. Chung: Binder-Assisted Injection Molding of Powders at the Rensselaer Symposium in Troy / New York from July 16 to 18, 1990.
- shortcomings of the wax-containing binder systems mentioned are already pointed out: low dimensional stability during thermal expulsion of the binder, long expulsion times, and a structural inhomogeneity of the green body after expulsion of the binder.
- New binder systems have therefore been developed which consist of a polymer component and a low molecular weight binder component which is solid at room temperature and which form solutions over a wide range of temperatures and mixtures, so-called solid polymer solutions (SPS). Compared to wax-containing SPS binder systems, they have the following advantages:
- the green bodies injection-molded therewith remain dimensionally stable while the binder is being driven out; after removal of the low-molecular component, a pore structure remains in the green compact, through which the gaseous crack products of the polymer component can escape; the low molecular weight component can be easily driven out and recovered below the melting point of the binder system.
- PLC binder systems are e.g. B. from the above-mentioned Vorschriftmanu ⁇ script by Chan I. Chung known, for example a system of 70% acetanilide, 20 ⁇ polymer and 10 " ⁇ stearic acid.
- the known SPS binder systems based on polystyrene or polyvinyl acetate and low molecular weight compounds such as acetanilide, diphenyl sulfone, diphenyl carbonate, antipyrine, naphthalene or decalin have the disadvantage that the low molecular weight components are harmful to health and therefore cannot be used everywhere for occupational safety reasons are.
- the known Binder systems wetting aids such. B. stearic acid. This is necessary for the fluidity of the compounds, but it is the cause of some difficulties in the process.
- binder systems according to the invention are based on non-toxic low molecular weight components and the polymer components are selected so that wetting aids such as, for. B. stearic acid are not necessary.
- wetting aids such as, for. B. stearic acid are not necessary.
- Cyclododecane, cyclododecanone, cyclododecanol or stearyl alcohol are suitable as low molecular weight components.
- cyclododecane is used as the low molecular weight component.
- Cyclododecane melts at 60 ° C, is largely physiologically harmless and can be removed very easily and quickly, by sublimation or by evaporation from the molding. It forms homogeneous melts with polyolefins below their solidification temperature.
- a relatively low viscosity polypropylene can e.g. B. can be obtained by oxidative degradation of most commercially available types of polypropylene.
- the binder system can easily be adapted for metal powders of different grain sizes and for different molded parts.
- Polypropylenes that are oxidatively degraded in air contain polar groups. They wet the metal powders coated with an oxide skin better than unmodified polypropylenes with the same flow index. This eliminates the need to add wetting aids.
- the binary binder system according to the invention is compounded with metal powders under protective gas in a kneader. The protective gas atmosphere during compounding prevents the oxidative dehydrogenation of the polymer component, which is catalyzed by many metal powders. When compounded in air, a partially dehydrated polypropylene would result. This results in inadmissibly high residual carbon contents when cracking under protective gas in the metal powder structure, which lead to structural defects during sintering, such as e.g. B. Carbide formation at the grain boundaries, voids and cracks due to methane formation.
- the residual carbon content in the sintered parts can be set in a wide range as desired and z. B. lower than 0.01% if desired.
- the pyrolysis time is therefore shorter than with the conventional temperature-time step functions.
- the additional preheating of the incoming protective gas makes the temperature in cracking and sintering furnaces more uniform. This reduces the time required for the thermal expulsion of the binder and the distortion of filigree molded parts during sintering.
- a commercially available type of polypropylene is oxidatively degraded by mastification at 200 ° C in air to a flow index 190 / 1.2 of 20 g per 10 minutes.
- low-boiling degradation products escape, which form during the oxidation of additives, such as stabilizers.
- the preparation takes place under protective gas, at 180 ° C. in a vacuum-tight SIGMA kneader, which was thoroughly rinsed with protective gas before heating.
- the compound granulates on its own during cooling while the kneader is running.
- the granules are processed into moldings in an extruder.
- Sintering takes place in several stages: first heating for three hours at 120 ° C in a gentle N stream to remove the cyclododecane, heating at 120 ° C / h under N stream to 260 ° C, heating at 20 ° C / h under N stream to 330 ° C, heating at 10 ° C / h under N flow to 430 ° C, rapid heating under H flow to 1280 ° C and 1.5 hours at 1280 ° C. Parts made in this way from 430 L steel powder had densities of 98.5% of the theoretically possible density.
- polystyrene resin In addition to polypropylenes, other polyolefins or copolymers of olefins with polar monomers in combination with cyclododecane are of course also suitable as binders for the MIM process.
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Powder Metallurgy (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4033952 | 1990-10-25 | ||
DE4033952A DE4033952C1 (enrdf_load_stackoverflow) | 1990-10-25 | 1990-10-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0554272A1 true EP0554272A1 (de) | 1993-08-11 |
Family
ID=6417038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP91917354A Withdrawn EP0554272A1 (de) | 1990-10-25 | 1991-10-10 | Bindersystem und verfahren für die verarbeitung von metallpulver durch spritzgiessen |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0554272A1 (enrdf_load_stackoverflow) |
JP (1) | JPH06501985A (enrdf_load_stackoverflow) |
DE (1) | DE4033952C1 (enrdf_load_stackoverflow) |
WO (1) | WO1992007675A1 (enrdf_load_stackoverflow) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4230376C1 (enrdf_load_stackoverflow) * | 1992-09-11 | 1993-04-22 | Robert Bosch Gmbh, 7000 Stuttgart, De | |
FR2705596B1 (fr) * | 1993-05-24 | 1995-07-13 | Impac Technologies | Procédé de moulage par injection de barbotines et dispositif pour sa mise en Óoeuvre. |
JPH07173503A (ja) * | 1993-11-04 | 1995-07-11 | Kobe Steel Ltd | 粉末冶金用結合剤および粉末冶金用混合粉末 |
DE4434471C1 (de) * | 1994-09-27 | 1996-03-28 | Bosch Gmbh Robert | Verfahren zur Herstellung von Formkörpern aus Hartferriten |
DE102007039246A1 (de) | 2007-08-20 | 2009-02-26 | Robert Bosch Gmbh | Formmasse und Verfahren zur Herstellung einer Formmasse |
WO2009027837A2 (en) * | 2007-08-28 | 2009-03-05 | Corning Incorporated | Method for making porous ceramic articles with fugitive pore former |
EP2030957A1 (en) * | 2007-08-28 | 2009-03-04 | Corning Incorporated | Fugitive pore former for porous ceramic articles |
DE102011089240A1 (de) | 2011-12-20 | 2013-06-20 | Robert Bosch Gmbh | Brennstoffeinspritzventil und Verfahren zur Ausformung von Abspritzöffnungen |
EP4058291A4 (en) * | 2019-11-15 | 2023-11-22 | Desktop Metal, Inc. | THERMAL UNBINDING TECHNIQUES FOR ADDITIVE MANUFACTURING, AND ASSOCIATED SYSTEMS AND METHODS |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3881283T2 (de) * | 1987-06-25 | 1993-11-18 | Idemitsu Petrochemical Co | Metallbinder und Zusammensetzung für die Guss-Formung. |
JPH0222165A (ja) * | 1988-07-08 | 1990-01-25 | Idemitsu Petrochem Co Ltd | セラミックスバインダー |
-
1990
- 1990-10-25 DE DE4033952A patent/DE4033952C1/de not_active Expired - Lifetime
-
1991
- 1991-10-10 EP EP91917354A patent/EP0554272A1/de not_active Withdrawn
- 1991-10-10 WO PCT/DE1991/000799 patent/WO1992007675A1/de not_active Application Discontinuation
- 1991-10-10 JP JP3515730A patent/JPH06501985A/ja active Pending
Non-Patent Citations (1)
Title |
---|
See references of WO9207675A1 * |
Also Published As
Publication number | Publication date |
---|---|
DE4033952C1 (enrdf_load_stackoverflow) | 1992-05-27 |
WO1992007675A1 (de) | 1992-05-14 |
JPH06501985A (ja) | 1994-03-03 |
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Legal Events
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PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
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17P | Request for examination filed |
Effective date: 19930320 |
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AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): CH DE ES FR GB IT LI SE |
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STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
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18D | Application deemed to be withdrawn |
Effective date: 19940430 |