JP2000160206A - Iron base powdery mixture for powder metallurgy and its production - Google Patents
Iron base powdery mixture for powder metallurgy and its productionInfo
- Publication number
- JP2000160206A JP2000160206A JP10238413A JP23841398A JP2000160206A JP 2000160206 A JP2000160206 A JP 2000160206A JP 10238413 A JP10238413 A JP 10238413A JP 23841398 A JP23841398 A JP 23841398A JP 2000160206 A JP2000160206 A JP 2000160206A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- acid amide
- weight
- mixture
- iron
- 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.)
- Granted
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 180
- 239000000203 mixture Substances 0.000 title claims abstract description 157
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 83
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 238000004663 powder metallurgy Methods 0.000 title claims description 33
- 239000000843 powder Substances 0.000 claims abstract description 229
- 239000000314 lubricant Substances 0.000 claims abstract description 99
- 229920005992 thermoplastic resin Polymers 0.000 claims abstract description 52
- -1 acrylic ester Chemical class 0.000 claims abstract description 42
- 238000000034 method Methods 0.000 claims abstract description 25
- 229920002554 vinyl polymer Polymers 0.000 claims abstract description 6
- 239000002245 particle Substances 0.000 claims description 60
- 238000002844 melting Methods 0.000 claims description 41
- 230000008018 melting Effects 0.000 claims description 41
- WGOROJDSDNILMB-UHFFFAOYSA-N octatriacontanediamide Chemical compound NC(=O)CCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCCC(N)=O WGOROJDSDNILMB-UHFFFAOYSA-N 0.000 claims description 40
- LYRFLYHAGKPMFH-UHFFFAOYSA-N octadecanamide Chemical compound CCCCCCCCCCCCCCCCCC(N)=O LYRFLYHAGKPMFH-UHFFFAOYSA-N 0.000 claims description 38
- 239000000178 monomer Substances 0.000 claims description 36
- 238000002156 mixing Methods 0.000 claims description 29
- 229910045601 alloy Inorganic materials 0.000 claims description 28
- 239000000956 alloy Substances 0.000 claims description 28
- 239000004698 Polyethylene Substances 0.000 claims description 18
- 235000021355 Stearic acid Nutrition 0.000 claims description 18
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 18
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 18
- 229920000573 polyethylene Polymers 0.000 claims description 18
- 239000008117 stearic acid Substances 0.000 claims description 18
- FATBGEAMYMYZAF-KTKRTIGZSA-N oleamide Chemical compound CCCCCCCC\C=C/CCCCCCCC(N)=O FATBGEAMYMYZAF-KTKRTIGZSA-N 0.000 claims description 17
- 230000002776 aggregation Effects 0.000 claims description 12
- 239000010687 lubricating oil Substances 0.000 claims description 12
- 150000001252 acrylic acid derivatives Chemical class 0.000 claims description 10
- 150000002734 metacrylic acid derivatives Chemical class 0.000 claims description 10
- 238000004220 aggregation Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000012803 melt mixture Substances 0.000 claims description 8
- 239000003921 oil Substances 0.000 claims description 8
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 8
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 8
- 238000005275 alloying Methods 0.000 claims description 6
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 5
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 5
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 5
- 239000005642 Oleic acid Substances 0.000 claims description 5
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 5
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 5
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 5
- 239000010723 turbine oil Substances 0.000 claims description 5
- 238000005054 agglomeration Methods 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000005245 sintering Methods 0.000 abstract description 6
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 abstract description 3
- 150000002505 iron Chemical class 0.000 abstract 1
- 239000011230 binding agent Substances 0.000 description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 15
- 229910052751 metal Inorganic materials 0.000 description 15
- 239000002184 metal Substances 0.000 description 13
- XOOUIPVCVHRTMJ-UHFFFAOYSA-L zinc stearate Chemical compound [Zn+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O XOOUIPVCVHRTMJ-UHFFFAOYSA-L 0.000 description 11
- 239000011812 mixed powder Substances 0.000 description 10
- 239000000047 product Substances 0.000 description 10
- 238000005204 segregation Methods 0.000 description 10
- 230000007423 decrease Effects 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 8
- ZJOLCKGSXLIVAA-UHFFFAOYSA-N ethene;octadecanamide Chemical compound C=C.CCCCCCCCCCCCCCCCCC(N)=O.CCCCCCCCCCCCCCCCCC(N)=O ZJOLCKGSXLIVAA-UHFFFAOYSA-N 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 8
- 239000011164 primary particle Substances 0.000 description 8
- 229920005989 resin Polymers 0.000 description 7
- 239000011347 resin Substances 0.000 description 7
- 238000000465 moulding Methods 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 5
- 239000000654 additive Substances 0.000 description 5
- 235000014113 dietary fatty acids Nutrition 0.000 description 5
- 239000000194 fatty acid Substances 0.000 description 5
- 229930195729 fatty acid Natural products 0.000 description 5
- HGPXWXLYXNVULB-UHFFFAOYSA-M lithium stearate Chemical compound [Li+].CCCCCCCCCCCCCCCCCC([O-])=O HGPXWXLYXNVULB-UHFFFAOYSA-M 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000004094 surface-active agent Substances 0.000 description 5
- MYRTYDVEIRVNKP-UHFFFAOYSA-N 1,2-Divinylbenzene Chemical compound C=CC1=CC=CC=C1C=C MYRTYDVEIRVNKP-UHFFFAOYSA-N 0.000 description 4
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 4
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- 150000004665 fatty acids Chemical class 0.000 description 4
- 239000000344 soap Substances 0.000 description 4
- 239000004071 soot Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229910000967 As alloy Inorganic materials 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 3
- 229910052799 carbon Inorganic materials 0.000 description 3
- 230000015271 coagulation Effects 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 239000002270 dispersing agent Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000011156 evaluation Methods 0.000 description 3
- 239000007870 radical polymerization initiator Substances 0.000 description 3
- 230000000087 stabilizing effect Effects 0.000 description 3
- 238000010558 suspension polymerization method Methods 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- GOXQRTZXKQZDDN-UHFFFAOYSA-N 2-Ethylhexyl acrylate Chemical compound CCCCC(CC)COC(=O)C=C GOXQRTZXKQZDDN-UHFFFAOYSA-N 0.000 description 2
- CFVWNXQPGQOHRJ-UHFFFAOYSA-N 2-methylpropyl prop-2-enoate Chemical compound CC(C)COC(=O)C=C CFVWNXQPGQOHRJ-UHFFFAOYSA-N 0.000 description 2
- KUDUQBURMYMBIJ-UHFFFAOYSA-N 2-prop-2-enoyloxyethyl prop-2-enoate Chemical compound C=CC(=O)OCCOC(=O)C=C KUDUQBURMYMBIJ-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 150000008051 alkyl sulfates Chemical class 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- KBLWLMPSVYBVDK-UHFFFAOYSA-N cyclohexyl prop-2-enoate Chemical compound C=CC(=O)OC1CCCCC1 KBLWLMPSVYBVDK-UHFFFAOYSA-N 0.000 description 2
- ZSWFCLXCOIISFI-UHFFFAOYSA-N cyclopentadiene Chemical compound C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- 150000001991 dicarboxylic acids Chemical class 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 238000010556 emulsion polymerization method Methods 0.000 description 2
- 230000001747 exhibiting effect Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- NKHAVTQWNUWKEO-UHFFFAOYSA-N fumaric acid monomethyl ester Natural products COC(=O)C=CC(O)=O NKHAVTQWNUWKEO-UHFFFAOYSA-N 0.000 description 2
- LNMQRPPRQDGUDR-UHFFFAOYSA-N hexyl prop-2-enoate Chemical compound CCCCCCOC(=O)C=C LNMQRPPRQDGUDR-UHFFFAOYSA-N 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- VAKIVKMUBMZANL-UHFFFAOYSA-N iron phosphide Chemical compound P.[Fe].[Fe].[Fe] VAKIVKMUBMZANL-UHFFFAOYSA-N 0.000 description 2
- 125000005397 methacrylic acid ester group Chemical group 0.000 description 2
- 125000005395 methacrylic acid group Chemical group 0.000 description 2
- ANISOHQJBAQUQP-UHFFFAOYSA-N octyl prop-2-enoate Chemical compound CCCCCCCCOC(=O)C=C ANISOHQJBAQUQP-UHFFFAOYSA-N 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 230000003405 preventing effect Effects 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- LYBIZMNPXTXVMV-UHFFFAOYSA-N propan-2-yl prop-2-enoate Chemical compound CC(C)OC(=O)C=C LYBIZMNPXTXVMV-UHFFFAOYSA-N 0.000 description 2
- PNXMTCDJUBJHQJ-UHFFFAOYSA-N propyl prop-2-enoate Chemical compound CCCOC(=O)C=C PNXMTCDJUBJHQJ-UHFFFAOYSA-N 0.000 description 2
- 241000894007 species Species 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
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- 239000004416 thermosoftening plastic Substances 0.000 description 2
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 2
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical class OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 1
- PRBHEGAFLDMLAL-GQCTYLIASA-N (4e)-hexa-1,4-diene Chemical compound C\C=C\CC=C PRBHEGAFLDMLAL-GQCTYLIASA-N 0.000 description 1
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- PMJHHCWVYXUKFD-SNAWJCMRSA-N (E)-1,3-pentadiene Chemical compound C\C=C\C=C PMJHHCWVYXUKFD-SNAWJCMRSA-N 0.000 description 1
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- XLYMOEINVGRTEX-ONEGZZNKSA-N (e)-4-ethoxy-4-oxobut-2-enoic acid Chemical compound CCOC(=O)\C=C\C(O)=O XLYMOEINVGRTEX-ONEGZZNKSA-N 0.000 description 1
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- SFUDBXKBPOKIIW-ARJAWSKDSA-N 1-o-ethyl 4-o-(oxiran-2-ylmethyl) (z)-but-2-enedioate Chemical compound CCOC(=O)\C=C/C(=O)OCC1CO1 SFUDBXKBPOKIIW-ARJAWSKDSA-N 0.000 description 1
- ARNSVGUHSKJJNE-UHFFFAOYSA-N 1-o-methyl 4-o-(oxiran-2-ylmethyl) 2-methylidenebutanedioate Chemical compound COC(=O)C(=C)CC(=O)OCC1CO1 ARNSVGUHSKJJNE-UHFFFAOYSA-N 0.000 description 1
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- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
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- MKTOIPPVFPJEQO-UHFFFAOYSA-N 4-(3-carboxypropanoylperoxy)-4-oxobutanoic acid Chemical compound OC(=O)CCC(=O)OOC(=O)CCC(O)=O MKTOIPPVFPJEQO-UHFFFAOYSA-N 0.000 description 1
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- OIYTYGOUZOARSH-UHFFFAOYSA-N 4-methoxy-2-methylidene-4-oxobutanoic acid Chemical compound COC(=O)CC(=C)C(O)=O OIYTYGOUZOARSH-UHFFFAOYSA-N 0.000 description 1
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- GCNKJQRMNYNDBI-UHFFFAOYSA-N [2-(hydroxymethyl)-2-(2-methylprop-2-enoyloxymethyl)butyl] 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OCC(CO)(CC)COC(=O)C(C)=C GCNKJQRMNYNDBI-UHFFFAOYSA-N 0.000 description 1
- TUOBEAZXHLTYLF-UHFFFAOYSA-N [2-(hydroxymethyl)-2-(prop-2-enoyloxymethyl)butyl] prop-2-enoate Chemical compound C=CC(=O)OCC(CO)(CC)COC(=O)C=C TUOBEAZXHLTYLF-UHFFFAOYSA-N 0.000 description 1
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- 150000005215 alkyl ethers Chemical class 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 125000005037 alkyl phenyl group Chemical group 0.000 description 1
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- 229940056585 ammonium laurate Drugs 0.000 description 1
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- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
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- 239000003093 cationic surfactant Substances 0.000 description 1
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- YMKDRGPMQRFJGP-UHFFFAOYSA-M cetylpyridinium chloride Chemical compound [Cl-].CCCCCCCCCCCCCCCC[N+]1=CC=CC=C1 YMKDRGPMQRFJGP-UHFFFAOYSA-M 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
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- 238000007599 discharging Methods 0.000 description 1
- RZMWTGFSAMRLQH-UHFFFAOYSA-L disodium;2,2-dihexyl-3-sulfobutanedioate Chemical compound [Na+].[Na+].CCCCCCC(C([O-])=O)(C(C([O-])=O)S(O)(=O)=O)CCCCCC RZMWTGFSAMRLQH-UHFFFAOYSA-L 0.000 description 1
- YHAIUSTWZPMYGG-UHFFFAOYSA-L disodium;2,2-dioctyl-3-sulfobutanedioate Chemical compound [Na+].[Na+].CCCCCCCCC(C([O-])=O)(C(C([O-])=O)S(O)(=O)=O)CCCCCCCC YHAIUSTWZPMYGG-UHFFFAOYSA-L 0.000 description 1
- 238000012674 dispersion polymerization Methods 0.000 description 1
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 1
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- 229940005650 monomethyl fumarate Drugs 0.000 description 1
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- 239000002736 nonionic surfactant Substances 0.000 description 1
- 150000001451 organic peroxides Chemical class 0.000 description 1
- JFHBKKGEVRVZPE-UHFFFAOYSA-N oxiran-2-ylmethyl 4-ethenylbenzoate Chemical compound C1=CC(C=C)=CC=C1C(=O)OCC1OC1 JFHBKKGEVRVZPE-UHFFFAOYSA-N 0.000 description 1
- YCNNCJXFNCVEOL-UHFFFAOYSA-N oxiran-2-ylmethyl ethenesulfonate Chemical compound C=CS(=O)(=O)OCC1CO1 YCNNCJXFNCVEOL-UHFFFAOYSA-N 0.000 description 1
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- 239000000088 plastic resin Substances 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
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- 235000019422 polyvinyl alcohol Nutrition 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 229940114930 potassium stearate Drugs 0.000 description 1
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- ANBFRLKBEIFNQU-UHFFFAOYSA-M potassium;octadecanoate Chemical compound [K+].CCCCCCCCCCCCCCCCCC([O-])=O ANBFRLKBEIFNQU-UHFFFAOYSA-M 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
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- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000004445 quantitative analysis Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
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- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 1
- 235000019333 sodium laurylsulphate Nutrition 0.000 description 1
- 229950005425 sodium myristyl sulfate Drugs 0.000 description 1
- UPUIQOIQVMNQAP-UHFFFAOYSA-M sodium;tetradecyl sulfate Chemical compound [Na+].CCCCCCCCCCCCCCOS([O-])(=O)=O UPUIQOIQVMNQAP-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000001593 sorbitan monooleate Substances 0.000 description 1
- 235000011069 sorbitan monooleate Nutrition 0.000 description 1
- 229940035049 sorbitan monooleate Drugs 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- OPQYOFWUFGEMRZ-UHFFFAOYSA-N tert-butyl 2,2-dimethylpropaneperoxoate Chemical compound CC(C)(C)OOC(=O)C(C)(C)C OPQYOFWUFGEMRZ-UHFFFAOYSA-N 0.000 description 1
- NMOALOSNPWTWRH-UHFFFAOYSA-N tert-butyl 7,7-dimethyloctaneperoxoate Chemical compound CC(C)(C)CCCCCC(=O)OOC(C)(C)C NMOALOSNPWTWRH-UHFFFAOYSA-N 0.000 description 1
- ISXSCDLOGDJUNJ-UHFFFAOYSA-N tert-butyl prop-2-enoate Chemical compound CC(C)(C)OC(=O)C=C ISXSCDLOGDJUNJ-UHFFFAOYSA-N 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- LDHQCZJRKDOVOX-UHFFFAOYSA-N trans-crotonic acid Natural products CC=CC(O)=O LDHQCZJRKDOVOX-UHFFFAOYSA-N 0.000 description 1
- PHYFQTYBJUILEZ-IUPFWZBJSA-N triolein Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(OC(=O)CCCCCCC\C=C/CCCCCCCC)COC(=O)CCCCCCC\C=C/CCCCCCCC PHYFQTYBJUILEZ-IUPFWZBJSA-N 0.000 description 1
- GRPURDFRFHUDSP-UHFFFAOYSA-N tris(prop-2-enyl) benzene-1,2,4-tricarboxylate Chemical compound C=CCOC(=O)C1=CC=C(C(=O)OCC=C)C(C(=O)OCC=C)=C1 GRPURDFRFHUDSP-UHFFFAOYSA-N 0.000 description 1
- KOZCZZVUFDCZGG-UHFFFAOYSA-N vinyl benzoate Chemical compound C=COC(=O)C1=CC=CC=C1 KOZCZZVUFDCZGG-UHFFFAOYSA-N 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Landscapes
- Powder Metallurgy (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、混合する潤滑剤に
金属成分を含まず、流動性やホッパからの流出性に優れ
た粉末冶金用鉄基粉末混合物及びその製造方法に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an iron-based powder mixture for powder metallurgy, which does not contain a metal component in a lubricant to be mixed and has excellent fluidity and outflow from a hopper, and a method for producing the same.
【0002】[0002]
【従来の技術】粉末冶金用鉄基粉末混合物は、ベースに
なる鉄基粉末としての鉄粉に、銅粉、黒鉛粉、燐化鉄粉
等の合金用粉末とステアリン酸亜鉛等の潤滑剤とを混合
し、さらに必要に応じて切削性改善用粉末を加えて製造
するのが一般的である。しかし、このような混合物は、
以下のような欠点を持っている。まず、その欠点は、こ
のような混合物が粒子径、形状、化学組成に関して、偏
析を生じ易いことである。つまり、該混合物は、大き
さ、形状及び密度の異なる複数種の粉末を含んでいるた
め、混合後の輸送、ホッパへの装入、払出し、又は金型
に充填して加圧成形処理等を行う際に、混合物の中で粒
子が均一に分布しなくなり、前記したような偏析が生じ
てしまう。例えば、鉄粉と黒鉛粉との混合物は、トラッ
ク輸送中の振動によって輸送容器内で鉄粉と黒鉛粉がそ
れぞれ勝手に運動、移動し、混合物内で均一分布しなく
なるため、偏析が生じ、特に、比重の小さい黒鉛粉が表
面に浮かび上がってくることは、良く知られている。ま
た、ホッパに装入された前記混合物は、ホッパ内の移動
で偏析を起こし、ホッパより排出された混合物は、排出
の初期、中期、終期でそれぞれ黒鉛粉濃度が異なってし
まうことも良く知られている。2. Description of the Related Art An iron-based powder mixture for powder metallurgy is prepared by adding an iron powder as a base iron powder, an alloy powder such as copper powder, graphite powder, iron phosphide powder and a lubricant such as zinc stearate. Is generally mixed, and if necessary, a powder for improving machinability is added. However, such a mixture
It has the following disadvantages. First, its disadvantage is that such mixtures tend to segregate in terms of particle size, shape and chemical composition. In other words, since the mixture contains a plurality of types of powders having different sizes, shapes and densities, transportation after mixing, charging into a hopper, discharging, or filling in a mold to perform a pressure molding process and the like. During the process, the particles are not uniformly distributed in the mixture, and the above-described segregation occurs. For example, in a mixture of iron powder and graphite powder, the iron powder and graphite powder move and move independently in the transport container due to vibration during truck transportation, and the powder is not uniformly distributed in the mixture. It is well known that graphite powder having a low specific gravity emerges on the surface. It is also well known that the mixture charged in the hopper segregates due to movement in the hopper, and the mixture discharged from the hopper has a different graphite powder concentration at the initial, middle and final stages of discharge. ing.
【0003】これら偏析を起こした混合物を、加圧(圧
縮)成形し、その成形体を焼結して最終製品である焼結
体を製造すると、該焼結体は、製品毎に組成がばらつい
たり、寸法及び強度も大きくばらつき、不良品が生じる
ことになる。また、混合する銅粉、黒鉛粉、燐化鉄粉等
は、いずれも鉄粉より微粉末であるため、混合物の比表
面積を増大させ、その流動性を低下させる。このような
混合物の流動性低下は、該混合物の成形用金型への充填
速度を低下させるので、成型体(圧粉体ともいう)の生
産速度を低下させる原因になる。[0003] When the segregated mixture is molded under pressure (compression) and the molded body is sintered to produce a sintered body as a final product, the composition of the sintered body varies from product to product. In addition, the size and strength vary greatly, resulting in defective products. Further, the copper powder, graphite powder, iron phosphide powder and the like to be mixed are all finer than iron powder, so that the specific surface area of the mixture is increased and its fluidity is reduced. Such a decrease in the fluidity of the mixture lowers the filling rate of the mixture into a molding die, which causes a reduction in the production rate of a molded body (also referred to as a green compact).
【0004】かかる混合物の偏析を防止するため、特公
平5−27682号公報は、鉄基粉末と、少なくとも1
種類の合金用粉末及び前記鉄基粉末並びに合金用粉末の
ための結合剤とを含む組成物であって、該組成物が、前
記鉄基粉末と合金粉末とに前記の結合剤を機械的に混合
することによって形成されたものである改善された組成
物において、前記結合剤がメタクリルポリマーで、水に
実質的に不溶の樹脂であり、且つ前記結合剤を約0.0
05ないし1.0重量%含むことを特徴とする粉末組成
物を開示している。また、その公報の「発明の詳細な説
明」には、メタクリルポリマーとして、メチルメタクリ
レートのホモポリマー(ポリメタクリル酸メチル)を開
示している。しかしながら、この特公平5−27682
号公報記載の混合物は、ポリメタクリル酸メチルを鉄基
粉末に合金用粉末を付着させる結合剤として含むのであ
って、粉末として含むものではないので、結合剤として
のポリメタクリル酸メチルは、当然偏析を防止できる
が、ホッパからの排出性(以下、単にホッパ排出性とい
う)が不十分で、それを向上させる必要があった。ま
た、結合剤として液状の樹脂を有機溶剤で溶かして鉄基
粉末表面を薄く被覆するので、有機溶剤の回収コストが
増加するという別の問題があった。[0004] In order to prevent the segregation of such a mixture, Japanese Patent Publication No. 5-27682 discloses an iron-based powder containing at least one powder.
Kind Code: A1 A composition comprising a powder for alloys and a binder for the iron-based powder and alloy powder, wherein the composition mechanically adds the binder to the iron-based powder and the alloy powder. An improved composition, formed by mixing, wherein the binder is a methacrylic polymer, a resin substantially insoluble in water, and wherein the binder is about 0.04%.
Disclosed is a powder composition characterized in that it contains from 0.05 to 1.0% by weight. Further, the detailed description of the invention in the publication discloses a homopolymer of methyl methacrylate (polymethyl methacrylate) as a methacrylic polymer. However, this Japanese Patent Publication 5-27682
The mixture described in the above publication contains polymethyl methacrylate as a binder for adhering the alloy powder to the iron-based powder, but not as a powder, so that polymethyl methacrylate as a binder naturally segregates. Can be prevented, but the dischargeability from the hopper (hereinafter simply referred to as hopper dischargeability) is insufficient, and it is necessary to improve it. Another problem is that the cost of recovering the organic solvent is increased because the surface of the iron-based powder is thinly coated by dissolving the liquid resin as a binder with an organic solvent.
【0005】前記とは別の偏析防止技術として、特開平
1−219101号公報は、ステアリン酸亜鉛を結合剤
にして鉄基粉末表面に黒鉛粉を付着させた混合粉末を開
示している。また、本発明者らは、先に特開平3−16
2502号において、金属石鹸と脂肪酸とを結合剤とし
て用いる方法を提案した。しかしながら、これら公報記
載の混合物は、いずれも結合剤に亜鉛やその他の金属元
素を含んでおり、成形体の焼結時に結合剤中の金属元素
が酸化物となって、焼結炉の内部を汚染したり、焼結体
の化学組成を変化させてしまうという問題点を有してい
た。そこで、かかる問題点を解決する方法として、特公
表昭60−502158号公報や特開平2−21740
3号公報は、金属元素を含まない結合剤を用いた混合物
を提案した。しかしながら、かかる公報記載の技術も、
結合剤自体が潤滑作用を持たないので、最終的にはステ
アリン酸亜鉛を潤滑剤として添加しており、上述のホッ
パ排出性問題を解決していなかった。As another segregation preventing technique, Japanese Patent Application Laid-Open No. 1-219101 discloses a mixed powder in which zinc stearate is used as a binder and graphite powder is adhered to the surface of an iron-based powder. Further, the present inventors have previously described in Japanese Patent Laid-Open No.
No. 2502 proposed a method using a metal soap and a fatty acid as a binder. However, the mixtures described in these publications all contain zinc and other metal elements in the binder, and the metal elements in the binder become oxides during sintering of the molded body, so that the inside of the sintering furnace is There were problems such as contamination and a change in the chemical composition of the sintered body. Therefore, as a method of solving such a problem, Japanese Patent Publication No. 60-502158 and Japanese Patent Laid-Open No. 21740/1990 are known.
No. 3 proposed a mixture using a binder containing no metal element. However, the technology described in this publication also
Since the binder itself has no lubricating action, zinc stearate is finally added as a lubricant, and the above-mentioned problem of hopper discharge property has not been solved.
【0006】これらの問題を踏まえて、本発明者らは、
先に特開平5−148505号公報にその解決策を開示
した。すなわち、ステアリン酸、オレイン酸アミド、ス
テアリン酸アミド、ステアリン酸アミドとエチレンビス
ステアリン酸アミドとの溶融混合物、エチレンビスステ
アリン酸アミドから選ばれた1種以上の結合剤と、合金
用粉末等及び鉄基粉末とを混合、加熱した後に冷却し
て、固化した結合剤で合金用粉末等を鉄基粉末に固着さ
せた上で、さらに、これに上記結合剤と同種の粉末とス
テアリン酸亜鉛等の粉末を潤滑剤として添加、混合した
粉末冶金用鉄基混合物及びその製造方法を提案した。ま
た、結合剤として高級脂肪酸、高級脂肪酸アミド、ワッ
クス、ステアリン酸亜鉛の加熱溶融物を使用する場合に
は、潤滑剤としてステアリン酸リチウムを使用すべきこ
とをも提案した。しかしながら、かかる技術によって
も、依然として少量のステアリン酸亜鉛や、ステアリン
酸リチウムなどの金属石鹸が配合されているため、完全
に焼結炉の内部汚染を解消することはできなかった。そ
の理由は、ステアリン酸亜鉛やステアリン酸リチウム等
の金属石鹸を含まない、つまり金属成分を含まない有機
物質のみからなる潤滑剤を用いた場合、得られた鉄基粉
末混合物の流動性やホッパ排出性が悪化するためであ
る。[0006] In view of these problems, the present inventors have:
The solution has been disclosed in Japanese Patent Application Laid-Open No. 5-148505. That is, stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, one or more binders selected from ethylenebisstearic acid amide, alloy powder, iron The base powder is mixed, heated and then cooled, and the alloy powder and the like are fixed to the iron base powder with the solidified binder, and further, the same kind of powder as the above binder and zinc stearate. An iron-based mixture for powder metallurgy, in which powder was added and mixed as a lubricant, and a method for producing the same were proposed. It has also been suggested that when a hot melt of higher fatty acids, higher fatty acid amides, waxes and zinc stearate is used as the binder, lithium stearate should be used as the lubricant. However, even with such a technique, since a small amount of metal soap such as zinc stearate or lithium stearate is still blended, the internal contamination of the sintering furnace could not be completely eliminated. The reason is that when a lubricant containing no metal soap such as zinc stearate or lithium stearate is used, that is, a lubricant consisting of only an organic substance containing no metal component is used, the fluidity and hopper discharge of the obtained iron-based powder mixture are reduced. This is because the sex deteriorates.
【0007】本発明は、かかる事情に鑑み、焼結炉の内
部を汚染する金属成分を含まない潤滑剤を用い、流動性
やホッパ排出性に優れた鉄基粉末混合物及びその製造方
法を提供することを目的としている。The present invention has been made in view of the above circumstances, and provides an iron-based powder mixture excellent in fluidity and hopper dischargeability using a lubricant that does not contain metal components that contaminate the inside of a sintering furnace, and a method for producing the same. It is intended to be.
【0008】[0008]
【課題を解決するための手段】本発明者等は、上記目的
を達成するため、従来の粉末冶金用鉄基粉末混合物につ
いて見直し、後述の新しい知見を多々得た。そして、金
属成分を全く含まない有機物質のみからなる潤滑剤を用
いても、従来並みの粉体及び圧粉体の特性を十分に維持
でき、且つ流動性やホッパ排出性に優れた粉末が得られ
ることを確認し本発明を完成するに至った。Means for Solving the Problems In order to achieve the above object, the present inventors reviewed conventional iron-based powder mixtures for powder metallurgy and obtained many new findings described later. Even if a lubricant composed of only an organic substance containing no metal component is used, the powder and the compact can maintain the characteristics of the conventional powder sufficiently, and a powder having excellent fluidity and hopper discharge property can be obtained. It was confirmed that the present invention was completed, and the present invention was completed.
【0009】すなわち、本発明は、鉄基粉末と、アクリ
ル酸エステル、メタクリル酸エステル及び芳香族ビニル
化合物の中から選ばれた少なくとも1種の単量体単位を
50重量%以上含有し、1次平均粒径が0.03〜5μ
m、凝集平均粒径が5〜50μm、溶液比粘度法で測定
した平均分子量が3万〜500万の熱可塑性樹脂粉末を
遊離粉末として0.05重量%以上0.50重量%以下
とを含むことを特徴とする粉末冶金用鉄基粉末混合物で
ある。また、本発明は、鉄基粉末と、該鉄基粉末に付着
した下記の内から選ばれた1種以上の潤滑剤0.1重量
%以上1.0重量%以下と、前記潤滑剤により前記鉄基
粉末に付着した合金用粉末及び/又は切削性改善用粉末
と、アクリル酸エステル、メタクリル酸エステル及び芳
香族ビニル化合物の中から選ばれた少なくとも1種の単
量体単位を50重量%以上含有し、1次平均粒径が0.
03〜5μm、凝集平均粒径が5〜50μm、溶液比粘
度法で測定した平均分子量が3万〜500万の熱可塑性
樹脂粉末0.05重量%以上0.50重量%以下とを遊
離粉末として含むことを特徴とする粉末冶金用鉄基粉末
混合物である。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。That is, the present invention comprises an iron-based powder and at least 50% by weight of at least one monomer unit selected from acrylates, methacrylates and aromatic vinyl compounds. Average particle size 0.03-5μ
m, a thermoplastic resin powder having a coagulation average particle size of 5 to 50 μm and an average molecular weight of 30,000 to 5,000,000 as measured by a solution specific viscosity method as a free powder, containing from 0.05% by weight to 0.50% by weight. An iron-based powder mixture for powder metallurgy characterized by the following. In addition, the present invention provides an iron-based powder, 0.1% by weight or more and 1.0% by weight or less of one or more kinds of lubricants selected from the following attached to the iron-based powder; 50% by weight or more of an alloy powder and / or a machinability improving powder attached to the iron-based powder and at least one monomer unit selected from acrylates, methacrylates and aromatic vinyl compounds Containing, having a primary average particle size of 0.1.
A thermoplastic resin powder having a particle size of from 03 to 5 μm, an average particle diameter of aggregation of from 5 to 50 μm, and an average molecular weight of 30,000 to 5,000,000 as measured by a solution specific viscosity method is from 0.05% by weight to 0.50% by weight as a free powder. It is an iron-based powder mixture for powder metallurgy characterized by containing. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
【0010】そして、本発明は、上記粉末冶金用鉄基粉
末混合物に、さらに、下記の内から選ばれた1種以上の
潤滑剤の粉末0.5重量%以下を遊離粉末として含むこ
とを特徴とする粉末冶金用鉄基粉末混合物である。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。The present invention is characterized in that the iron-based powder mixture for powder metallurgy further contains 0.5% by weight or less of one or more lubricant powders selected from the following as free powder. Is an iron-based powder mixture for powder metallurgy. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
【0011】また、本発明は、上記粉末冶金用鉄基粉末
混合物に、さらに、オレイン酸、スピンドル油、タービ
ン油の内から選ばれた1種以上の有機質液体潤滑剤0.
01重量%以上0.3重量%以下を含むことを特徴とす
る粉末冶金用鉄基粉末混合物である。[0011] The present invention also relates to the iron-based powder mixture for powder metallurgy, further comprising at least one organic liquid lubricant selected from oleic acid, spindle oil and turbine oil.
It is an iron-based powder mixture for powder metallurgy characterized by containing not less than 01% by weight and not more than 0.3% by weight.
【0012】さらに、本発明は、鉄基粉末と、合金用粉
末及び/又は切削性改善用粉末と、下記の内から選ばれ
た1種以上の潤滑剤の粉末0.1重量%以上1.0重量
%以下と、アクリル酸エステル、メタクリル酸エステル
及び芳香族ビニル化合物の中から選ばれた少なくとも1
種の単量体単位を50重量%以上含有し、1次平均粒径
が0.03〜5μm、凝集平均粒径が5〜50μm、溶
液比粘度法で測定した平均分子量が3万〜500万の熱
可塑性樹脂粉末0.05重量%以上0.50重量%以下
とを含むことを特徴とする粉末冶金用鉄基粉末混合物で
ある。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。Further, the present invention provides an iron-based powder, a powder for alloying and / or a powder for improving machinability, and a powder of at least 0.1% by weight of at least one lubricant selected from the following. 0% by weight or less and at least one selected from acrylates, methacrylates and aromatic vinyl compounds.
Containing 50% by weight or more of various kinds of monomer units, having a primary average particle size of 0.03 to 5 μm, an aggregation average particle size of 5 to 50 μm, and an average molecular weight of 30,000 to 5,000,000 as measured by a solution specific viscosity method. And 0.05 to 0.50% by weight of a thermoplastic resin powder of the present invention. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
【0013】さらに加えて、本発明は、前記熱可塑性樹
脂粉末が、ポリメタクリル酸メチルであることを特徴と
する粉末冶金用鉄基粉末混合物でもある。[0013] In addition, the present invention is also an iron-based powder mixture for powder metallurgy, wherein the thermoplastic resin powder is polymethyl methacrylate.
【0014】製造方法に関しても発明をなし、まず、本
発明は、鉄基粉末と、合金用粉末及び/又は切削性改善
用粉末と、下記の内から選ばれた1種以上の潤滑剤0.
1重量%以上1.0重量%以下とを混合した後、その混
合物を、さらに前記潤滑剤が1種の場合は、該潤滑剤の
融点より10℃以上100℃以下高い温度で、前記潤滑
剤が2種以上からなる場合は、該潤滑剤の最低の融点よ
り10℃以上高く最高の融点以下の温度で加熱しながら
混合し、少なくとも1種以上の潤滑剤を溶融させ、引き
続き冷却して、前記鉄基粉末に前記合金用粉末及び/又
は切削性改善用粉末を溶融した前記潤滑剤により付着し
た後、この付着後の混合物に、アクリル酸エステル、メ
タクリル酸エステル及び芳香族ビニル化合物の中から選
ばれた少なくとも1種の単量体単位を50重量%以上含
有し、1次平均粒径が0.03〜5μm、凝集平均粒径
が5〜50μm、溶液比粘度法で測定した平均分子量が
3万〜500万の熱可塑性樹脂粉末0.05重量%以上
0.50重量%以下を混合することを特徴とする粉末冶
金用鉄基粉末混合物の製造方法である。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。The invention also relates to a manufacturing method. First, the present invention relates to an iron-based powder, a powder for alloying and / or a powder for improving machinability, and one or more lubricants selected from the following.
After mixing 1% by weight or more and 1.0% by weight or less, the mixture is further mixed with the lubricant at a temperature higher than the melting point of the lubricant by 10 ° C or more and 100 ° C or less when one kind of the lubricant is used. Is composed of two or more kinds, mixing while heating at a temperature of 10 ° C. or more higher than the lowest melting point of the lubricant and not more than the highest melting point, melting at least one kind of the lubricant, and subsequently cooling, After the alloy powder and / or the powder for improving machinability are adhered to the iron-based powder by the molten lubricant, the mixture after the adhesion is selected from acrylates, methacrylates, and aromatic vinyl compounds. 50% by weight or more of at least one selected monomer unit, a primary average particle diameter of 0.03 to 5 μm, an aggregation average particle diameter of 5 to 50 μm, and an average molecular weight measured by a solution specific viscosity method. 30,000-5,000,000 heat A method for producing an iron-based powder mixture for powder metallurgy, comprising mixing 0.05% by weight or more and 0.50% by weight or less of a plastic resin powder. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
【0015】また、本発明は、鉄基粉末と、合金用粉末
及び/又は切削性改善用粉末と、下記の内から選ばれた
1種以上の潤滑剤0.1重量%以上1.0重量%以下
と、オレイン酸、スピンドル油、タービン油の内から選
ばれた1種以上の有機質液体潤滑剤0.01重量%以上
0.3重量%以下とを混合した後、その混合物を、前記
潤滑剤が1種の場合は、該潤滑剤の融点より10℃以上
100℃以下高い温度で加熱、混合し、前記潤滑剤が2
種以上からなる場合は、最低の融点の10℃以上最高の
融点以下の温度で加熱、混合し、少なくとも1種以上の
潤滑剤を溶融し、引き続き冷却して、前記鉄基粉末に前
記合金用粉末及び/又は切削性改善用粉末を溶融した前
記潤滑剤により付着した後、この付着処理後の混合物
に、アクリル酸エステル、メタクリル酸エステル及び芳
香族ビニル化合物の中から選ばれた少なくとも1種の単
量体単位を50重量%以上含有し、1次平均粒径が0.
03〜5μm、凝集平均粒径が5〜50μm、溶液比粘
度法で測定した平均分子量が3万〜500万の熱可塑性
樹脂粉末0.05重量%以上0.50重量%以下を混合
することを特徴とする粉末冶金用鉄基粉末混合物の製造
方法である。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。Further, the present invention provides an iron-based powder, an alloy powder and / or a machinability improving powder, and 0.1% by weight or more and 1.0% by weight or more of one or more kinds of lubricants selected from the following. % Or less and one or more organic liquid lubricants selected from among oleic acid, spindle oil and turbine oil in an amount of 0.01% by weight or more and 0.3% by weight or less. When one kind of the agent is used, the mixture is heated and mixed at a temperature higher than the melting point of the lubricant by 10 ° C. or more and 100 ° C. or less.
If it consists of more than one kind, it is heated and mixed at a temperature of 10 ° C. or more of the lowest melting point or more and the highest melting point or less, melts at least one kind of lubricant, and then cools it, After the powder and / or the machinability improving powder are adhered by the molten lubricant, the mixture after the adhesion treatment is added to at least one kind selected from acrylates, methacrylates and aromatic vinyl compounds. A monomer unit is contained in an amount of 50% by weight or more, and the primary average particle size is 0.1%.
A mixture of 0.05 to 0.50% by weight of a thermoplastic resin powder having an average molecular weight of 30,000 to 5,000,000 as measured by a solution specific viscosity method, having a mean particle size of from 3 to 5 μm, an aggregation average particle size of 5 to 50 μm. A method for producing an iron-based powder mixture for powder metallurgy, which is a feature of the present invention. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
【0016】さらに、本発明は、前記付着処理後の混合
物に、さらに、下記の内から選ばれた1種以上の潤滑剤
の粉末0.5重量%以下を加えて、混合することを特徴
とする粉末冶金用鉄基粉末混合物の製造方法でもある。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。Further, the present invention is characterized in that 0.5% by weight or less of powder of one or more lubricants selected from the following is further added to the mixture after the above-mentioned adhesion treatment and mixed. It is also a method for producing an iron-based powder mixture for powder metallurgy. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
【0017】さらに加えて、本発明は、前記熱可塑性樹
脂粉末が、ポリメタクリル酸メチルであることを特徴と
する粉末冶金用鉄基粉末混合物の製造方法でもある。Further, the present invention is also a method for producing an iron-based powder mixture for powder metallurgy, wherein the thermoplastic resin powder is polymethyl methacrylate.
【0018】[0018]
【発明の実施の形態】以下、本発明の実施の形態を詳細
に説明する。まず、本発明に係る粉末冶金用鉄基粉末混
合物(以下、単に本発明に係る混合物ということが多
い)は、鉄基粉末に、遊離粉末として、従来粉末冶金用
に使用されたことのない、アクリル酸エステル、メタク
リル酸エステル及び芳香族ビニル化合物の中から選ばれ
た少なくとも1種の単量体単位を50%以上含有し、そ
の一次平均粒径が0.03μm〜5μm、凝集平均粒径
が5〜50μm、平均分子量が3万〜500万の熱可塑
性樹脂粉末を0.05重量%以上0.50重量%以下混
合したことが大きなポイントである。これにより、該本
発明に係る混合物の流動性やホッパ排出性を、従来のも
のより改善できるからである。ここで、鉄基粉末として
は、鋼材の製造時に生成するミルスケールや鉄鉱石を還
元した還元鉄粉、溶鋼のアトマイズで製造した純鉄粉及
び/又は合金鉄粉が好ましい。それに混合する合金用粉
末としては、黒鉛粉末、銅粉、各種合金粉末等が用いら
れ、焼結体とした際に、その切削性を改善する切削性改
善用粉末としては、タルク、金属硫化物等が製品焼結体
に要求される特性を考慮して、選定される。なお、該合
金用粉末は、合計で5.0重量%以下の混合が好まし
く、該切削性改善用粉末は、合計で5.0重量%以下の
混合が好ましい。前記熱可塑性樹脂粉末を0.05%以
上0.5%以下配合するのは、添加量が0.05%未満
ではホッパ排出性が低下し、0.5%を超えると、圧縮
性が低下するためである。Embodiments of the present invention will be described below in detail. First, the iron-based powder mixture for powder metallurgy according to the present invention (hereinafter, often referred to simply as the mixture according to the present invention) is an iron-based powder, as a free powder, which has not been used for powder metallurgy in the past. 50% or more of at least one monomer unit selected from acrylic acid esters, methacrylic acid esters and aromatic vinyl compounds, having a primary average particle size of 0.03 μm to 5 μm and an aggregation average particle size of A significant point is that a thermoplastic resin powder having a particle size of 5 to 50 μm and an average molecular weight of 30,000 to 5,000,000 is mixed at 0.05% by weight or more and 0.50% by weight or less. Thereby, the fluidity and the hopper discharge property of the mixture according to the present invention can be improved as compared with the conventional one. Here, as the iron-based powder, mill scale generated during the production of steel materials, reduced iron powder obtained by reducing iron ore, pure iron powder and / or alloyed iron powder produced by atomizing molten steel is preferable. Graphite powder, copper powder, various alloy powders, etc. are used as the alloy powder to be mixed with the alloy powder. When the sintered body is formed, the machinability improving powder for improving the machinability is talc, metal sulfide, or the like. Are selected in consideration of the characteristics required for the product sintered body. The alloy powder is preferably mixed in a total of 5.0% by weight or less, and the machinability improving powder is preferably mixed in a total of 5.0% by weight or less. When the thermoplastic resin powder is blended in an amount of 0.05% or more and 0.5% or less, the hopper discharge property decreases when the addition amount is less than 0.05%, and the compressibility decreases when the addition amount exceeds 0.5%. That's why.
【0019】また、一次平均粒径とは、図1に示すよう
に、熱可塑性樹脂粉末の個々の粒子(一次粒子1とい
う)の平均値であり、それらが凝集して形成している凝
集粒子2の粒径の平均値ではない。具体的に、それは、
電子顕微鏡で凝集粒子2を観察して、所謂SEM写真を
取り、凝集粒子2を形成している一次粒子1の50個程
度の径(一次粒径3)を実測し、平均したものである。
また、凝集粒子2の平均粒径も、同様に、電子顕微鏡で
凝集粒径4を観察した結果(SEM写真)から定められ
る。なお、これらの粒径を上記の範囲に限定した理由
は、後述する。前記熱可塑性樹脂粉末としては、アクリ
ル酸エステル、メタクリル酸エステル及び芳香族ビニル
化合物の中から選ばれた少なくとも1種類の単量体単位
を50重量%以上含有することが好ましい。50重量%
未満であると、鉄基粉末用潤滑剤として使用した場合、
該熱可塑性樹脂粉末が混合物の流動性を十分に改善しな
い恐れがあるからである。また、これらの単量体は、1
種を単独でも、あるいは2種以上を組み合わせて用いて
も良い。The primary average particle size is an average value of individual particles (referred to as primary particles 1) of the thermoplastic resin powder as shown in FIG. 2 is not the average value of the particle diameters. Specifically, it
The so-called SEM photograph is taken by observing the aggregated particles 2 with an electron microscope, and the diameter (primary particle diameter 3) of about 50 primary particles 1 forming the aggregated particles 2 is actually measured and averaged.
Similarly, the average particle size of the aggregated particles 2 is also determined from the result of observing the aggregated particle size 4 with an electron microscope (SEM photograph). The reason for limiting the particle size to the above range will be described later. The thermoplastic resin powder preferably contains at least 50% by weight of at least one monomer unit selected from acrylates, methacrylates, and aromatic vinyl compounds. 50% by weight
If less than, when used as a lubricant for iron-based powder,
This is because the thermoplastic resin powder may not sufficiently improve the fluidity of the mixture. In addition, these monomers are 1
The species may be used alone or in combination of two or more.
【0020】該熱可塑性樹脂粉末の単量体単位としての
アクリル酸エステルとしては、例えば、メチルメタクリ
レート、エチルアクリレート、n−プロピルアクリレー
ト、イソプロピルアクリレート、n−ブチルアクリレー
ト、イソブチルアクリレート、sec−ブチルアクリレ
ート、t−ブチルアクリレート、n−ヘキシルアクリレ
ート、シクロヘキシルアクリレート、2−エチルヘキシ
ルアクリレート、n−オクチルアクリレート等を挙げる
ことができる。また、メタクリル酸エステルとしては、
例えば、メチルメタクリレート、エチルメタクリレー
ト、n−プロピルアクリレート、イソプロピルアクリレ
ート、n−ブチルアクリレート、イソブチルアクリレー
ト、n−ヘキシルアクリレート、シクロヘキシルアクリ
レート、2−エチルヘキシルアクリレート、n−オクチ
ルアクリレート等を挙げることができる。これらの単量
体の中で、特にメチルメタクリレートを好適に使用する
ことができる。The acrylic ester as a monomer unit of the thermoplastic resin powder includes, for example, methyl methacrylate, ethyl acrylate, n-propyl acrylate, isopropyl acrylate, n-butyl acrylate, isobutyl acrylate, sec-butyl acrylate, Examples include t-butyl acrylate, n-hexyl acrylate, cyclohexyl acrylate, 2-ethylhexyl acrylate, and n-octyl acrylate. Also, as methacrylic acid ester,
For example, methyl methacrylate, ethyl methacrylate, n-propyl acrylate, isopropyl acrylate, n-butyl acrylate, isobutyl acrylate, n-hexyl acrylate, cyclohexyl acrylate, 2-ethylhexyl acrylate, n-octyl acrylate and the like can be mentioned. Among these monomers, methyl methacrylate can be particularly preferably used.
【0021】さらに、芳香族ビニル化合物としては、例
えば、スチレン、α−メチルスチレン、ジビニルベンゼ
ン及びこれらの単量体のベンゼン核に、メチル基、エチ
ル基、プロピル基、ブチル基等が置換された単量体、例
えばビニルトルエンやイソブチルスチレン等を挙げるこ
とができる。Further, as the aromatic vinyl compound, for example, styrene, α-methylstyrene, divinylbenzene and the benzene nucleus of these monomers are substituted with methyl group, ethyl group, propyl group, butyl group and the like. Monomers such as vinyltoluene and isobutylstyrene can be exemplified.
【0022】以上3種の単量体単位と共重合可能な他の
単量体としては、例えば、アクリル酸、メタクリル酸、
2−エチルアクリル酸、クロトン酸、ケイ皮酸などの不
飽和モノカルボン酸;マレイン酸、イタコン酸、フマル
酸、シトラコン酸、クロロマレイン酸等の不飽和ジカル
ボン酸やその無水物:マレイン酸モノメチル、マレイン
酸モノブチル、フマル酸モノメチル、フマル酸モノエチ
ル、イタコン酸モノメチル、イタコン酸モノエチル、イ
タコン酸モノブチル等の不飽和ジカルボン酸のモノエス
テルやその誘導体;グリシジルメタクリレート、グリジ
ジルアクリレート、グリシジル−p−ビニルベンゾエー
ト、メチルグリシジルイタコネート、エチルグリシジル
マレエート、グリシジルビニルスルホネート、グリシジ
ルエーテル類;ブタジエンモノオキシド、ビニルシクロ
ヘキセンモノオキシド、5.6−エポキシヘキセン、2
−メチル−5.6−エポキシヘキセン等のエポキシドオ
レフィン類;アクリロニトリルやメタクリロニトリルな
どのシアン化ビニル類;酢酸ビニル、プロピオン酸ビニ
ル、ミリスチン酸ビニル、オレイン酸ビニル、安息香酸
ビニル等のビニルエステル類;ブタジエン、イソプレ
ン、1、3−ペンタジエン、シクロペンタジエン等の共
役ジエン系化合物;1、4−ヘキサジエン、ジシクロペ
ンタジエン、エチリデンノルボルネン等の非共役ジエン
系化合物を挙げることができる。また、共重合可能な単
量体として、反応性が実質上等しい2個以上の二重結合
を有する架橋性単量体を単量体全体の0.1〜2重量%
添加しても良い。そのような架橋性単量体を、単量体全
体の0.1〜2重量%添加するのが好ましい。そのよう
な架橋性単量体としては、エチレングリコールジアクリ
レート、エチレングリコールジメタクリレート、ブチレ
ングリコールジアクリレート、ブチレングリコールジメ
タクリレート、トリメチロールプロパンジアクリレー
ト、トリメチロールプロパンジメタクリレート、トリメ
チロールプロパントリアクリレート、トリメチロールプ
ロパントリメタクリレート、ヘキサンジオールジアクリ
レート、ヘキサンジオールジメタクリレート、オリゴキ
シエチレンジアクリレート、オリゴキシエチレンジメタ
クリレート、さらにはジビニルベンゼン等の芳香族ジビ
ニル単量体、トリメリット酸トリアリル、トリアリルイ
ソシアヌレート等を用いることができる。Other monomers copolymerizable with the above three types of monomer units include, for example, acrylic acid, methacrylic acid,
Unsaturated monocarboxylic acids such as 2-ethylacrylic acid, crotonic acid and cinnamic acid; unsaturated dicarboxylic acids such as maleic acid, itaconic acid, fumaric acid, citraconic acid and chloromaleic acid, and anhydrides thereof: monomethyl maleate; Monoesters and derivatives of unsaturated dicarboxylic acids such as monobutyl maleate, monomethyl fumarate, monoethyl fumarate, monomethyl itaconate, monoethyl itaconate and monobutyl itaconate; glycidyl methacrylate, glycidyl acrylate, glycidyl-p-vinylbenzoate; Methyl glycidyl itaconate, ethyl glycidyl maleate, glycidyl vinyl sulfonate, glycidyl ethers; butadiene monoxide, vinylcyclohexene monoxide, 5.6-epoxyhexene,
Epoxide olefins such as -methyl-5.6-epoxyhexene; vinyl cyanides such as acrylonitrile and methacrylonitrile; vinyl esters such as vinyl acetate, vinyl propionate, vinyl myristate, vinyl oleate and vinyl benzoate Conjugated diene compounds such as butadiene, isoprene, 1,3-pentadiene and cyclopentadiene; and non-conjugated diene compounds such as 1,4-hexadiene, dicyclopentadiene and ethylidene norbornene. Further, as a copolymerizable monomer, a crosslinkable monomer having two or more double bonds having substantially the same reactivity is used in an amount of 0.1 to 2% by weight of the whole monomer.
It may be added. It is preferable to add such a crosslinkable monomer in an amount of 0.1 to 2% by weight of the whole monomer. Such crosslinkable monomers include ethylene glycol diacrylate, ethylene glycol dimethacrylate, butylene glycol diacrylate, butylene glycol dimethacrylate, trimethylolpropane diacrylate, trimethylolpropane dimethacrylate, trimethylolpropane triacrylate, trimethylol Methylolpropane trimethacrylate, hexanediol diacrylate, hexanediol dimethacrylate, oligoxyethylene diacrylate, oligoxyethylene dimethacrylate, aromatic divinyl monomers such as divinylbenzene, triallyl trimellitate, triallyl isocyanurate, etc. Can be used.
【0023】本発明では、前記した熱可塑性樹脂粉末の
一次平均粒径(重量基準)を0.03〜5.0μmに限
定した。一次平均粒径が0.03μm未満であると、本
発明に係る混合物の製造コストが高くなり、工業製品へ
の応用に向かず、また、5.0μmを超えると、該混合
物を金型へ充填し、加圧成形して得られる成形体の密度
(以下、単に圧縮性という)が低下するからである。た
だし、実用上は、0.05〜3.0μmであることがよ
り好ましい。また、該樹脂粉末の凝集平均粒径は、5〜
50μmと限定している。凝集平均粒径が5μm以下と
なると、本発明に係る混合物の流動性やホッパ排出性が
低下し、50μmを超えると、該混合物の成形体を焼成
して得られる焼結体(以下、単に焼結体という)の引張
り強さが従来の混合物で得られる焼結体より低下するか
らである。ただし、この凝集平均粒径も、10〜40μ
mであることがより好ましい。さらに、該熱可塑性樹脂
粉末としては、平均単一粒径の異なる2種以上の熱可塑
性樹脂粉末を混合することができるが、その場合、前記
1次平均粒径としては、混合した粉末の総合重量基準の
平均値が0.03〜5.0μmになるように、混合比率
を調整することになる。In the present invention, the primary average particle size (by weight) of the thermoplastic resin powder is limited to 0.03 to 5.0 μm. If the primary average particle size is less than 0.03 μm, the production cost of the mixture according to the present invention increases, and the mixture is not suitable for application to industrial products. If it exceeds 5.0 μm, the mixture is filled into a mold. This is because the density (hereinafter, simply referred to as compressibility) of a molded article obtained by pressure molding decreases. However, in practical use, the thickness is more preferably 0.05 to 3.0 μm. The resin powder has an average coagulation particle size of 5 to 5.
It is limited to 50 μm. When the agglomeration average particle size is 5 μm or less, the fluidity and the hopper discharge property of the mixture according to the present invention decrease. This is because the tensile strength is lower than that of a sintered body obtained from a conventional mixture. However, the agglomerated average particle size is also 10 to 40 μm.
m is more preferable. Further, as the thermoplastic resin powder, two or more kinds of thermoplastic resin powders having different average single particle diameters can be mixed. In this case, the primary average particle diameter is defined as the total of the mixed powders. The mixing ratio is adjusted so that the weight-based average value is 0.03 to 5.0 μm.
【0024】加えて、本発明では、熱可塑性樹脂粉末
は、溶液比粘度法で測定した平均分子量が3万〜500
万の範囲に入るものに限定した。平均分子量が3万未満
だと、本発明に係る混合物の製造コストが高くなり過
ぎ、工業製品への応用に向かず、500万超えでは、該
混合物の流動性とホッパ排出性が従来品より低下するか
らである。ここに、溶液比粘度法とは、試料樹脂0.2
gをテトラヒドロフラン50mlに溶解し、該溶液の3
5℃における粘度を同温度の溶媒の粘度に対する比とし
て求め、平均分子量既知の各種標準ポリスチレンで予め
定めていた比粘度−平均分子量の関係から、該試料樹脂
の平均分子量を求める方法である。In addition, in the present invention, the thermoplastic resin powder has an average molecular weight of 30,000 to 500 measured by a solution specific viscosity method.
Limited to those within the range of 10,000. If the average molecular weight is less than 30,000, the production cost of the mixture according to the present invention becomes too high, and it is not suitable for application to industrial products. If it exceeds 5,000,000, the fluidity and hopper discharge property of the mixture are lower than conventional products. Because you do. Here, the solution specific viscosity method refers to a sample resin 0.2
g in 50 ml of tetrahydrofuran.
In this method, the viscosity at 5 ° C. is determined as a ratio to the viscosity of the solvent at the same temperature, and the average molecular weight of the sample resin is determined from the relationship of specific viscosity-average molecular weight predetermined by various standard polystyrenes having known average molecular weights.
【0025】さらに加えて、上記した熱可塑性樹脂粉末
の製造には、特に制限はなく、従来よりポリメチルメタ
クリレート等の微細樹脂粉末の製造に用いられている方
法、例えば、微細懸濁重合法、乳化重合法、播種乳化重
合法などを採用すれば良い。これらの方法の中でも、特
に、粒径が極微細とならず、且つ球形粒子が得られる重
合法が好適である。微細懸濁重合法としては、ラジカル
重合開始剤として油溶性開始剤を用い、重合開始前に単
量体油滴の粒径を均質化処理して予め調節し、均質分散
重合させる方法などが好適である。In addition, there is no particular limitation on the production of the above-mentioned thermoplastic resin powder, and methods conventionally used for producing fine resin powders such as polymethyl methacrylate, for example, fine suspension polymerization, An emulsion polymerization method, a seeded emulsion polymerization method, or the like may be employed. Among these methods, a polymerization method in which the particle size is not extremely fine and spherical particles are obtained is particularly preferable. As the fine suspension polymerization method, a method in which an oil-soluble initiator is used as a radical polymerization initiator, the particle size of monomer oil droplets is homogenized before the polymerization is started, and the particle size is adjusted in advance, and homogenous dispersion polymerization is preferably performed. It is.
【0026】油溶性のラジカル重合開始剤には、例え
ば、ベンゾイルパーオキサイド、ジ−3,5,5−トリ
メチルヘキサノイルパーオキサイド、ジラウロイルパー
オキサイド等のジアシルパーオキサイド類、ジイソプロ
ピルパーオキシジカ−ボネート、ジーsec−ブチルパ
ーオキシジカーボネート、ジ−2−エチルヘキシルパー
オキシジカーボネート等のパーオキシジカーボネート
類;t−ブチルパーオキシピバレート、t−ブチルパー
オキシネオデカノエート等のパーオキシエステル類、あ
るいはアセチルシクロヘキシルスルホニルパーオキサイ
ド、ジサクシニックアッシドパーオキサイド等の有機過
酸化物、さらには、2,2'−アゾビスイソブチロニト
リル、2,2'−アゾビス−2−メチルブチロニトリ
ル、2,2'−アゾビスジメチルバレロニトリル等のア
ゾ化合物などを使用することができる。また、これらの
ラジカル重合開始剤は、1種を単独でも、あるいは2種
以上を組み合わせて用いることもできる。その使用量
は、単量体の種類と量及び仕込方式などによって適宜選
択することができるが、通常、使用単量体100重量部
当り、0.001〜5.0重量部の範囲で使用すること
が好ましい。Examples of the oil-soluble radical polymerization initiator include diacyl peroxides such as benzoyl peroxide, di-3,5,5-trimethylhexanoyl peroxide and dilauroyl peroxide, and diisopropylperoxydicarbonate. Peroxydicarbonates such as di-sec-butylperoxydicarbonate and di-2-ethylhexylperoxydicarbonate; peroxyesters such as t-butylperoxypivalate and t-butylperoxyneodecanoate Or organic peroxides such as acetylcyclohexylsulfonyl peroxide and disuccinic acid peroxide; furthermore, 2,2′-azobisisobutyronitrile, 2,2′-azobis-2-methylbutyronitrile, , 2'-Azobisdim Or the like can be used azo compounds such as Le valeronitrile. These radical polymerization initiators can be used alone or in combination of two or more. The amount used can be appropriately selected depending on the type and amount of the monomer, the preparation method, and the like, but is usually used in the range of 0.001 to 5.0 parts by weight per 100 parts by weight of the monomer used. Is preferred.
【0027】微細懸濁重合法の実施に際しては、通常、
界面活性剤や分散剤が用いられるが、その界面活性剤と
しては、例えば、ラウリル硫酸エステルナトリウム、ミ
リスチル硫酸エステルナトリウム等のアルキル硫酸エス
テル塩類;ドデシルベンゼンスルホン酸ナトリウム、ド
デシルベンゼンスルホン酸カリウム等のアルキルアリー
ルスルホン酸塩類;ジオクチルスルホコハク酸ナトリウ
ム、ジヘキシルスルホコハク酸ナトリウム等のスルホコ
ハク酸エステル塩類;ラウリン酸アンモニウム、ステア
リン酸カリウム等の脂肪酸塩類;ポリオキシエチレンア
ルキル硫酸エステル塩類;ポリオキシエチレンアルキル
アリール硫酸エステル塩類;さらには、ドデシルジフェ
ニルエーテルジスルフォン酸ナトリウム等のアニオン性
界面活性剤類;ソルビタンモノオレエート、ポリオキシ
エチレンソルビタンモノステアレート等のソルビタンエ
ステル類;ポリオキシエチレンアルキルエーテル類;ポ
リオキシエチレンアルキルフェニルエーテル類等のノニ
オン性界面活性剤類;セチルピリジニウムクロライド、
セチルトリメチルアンモニウムブロマイド等のカチオン
性界面活性剤などを挙げることができる。また、分散剤
としては、ポリビニルアルコール、メチルセルロース、
ポリビニルピロリドン等を挙げることができる。これら
の界面活性剤や分散剤は、1種を単独でも、あるいは2
種以上を組み合わせて用いても良い。その使用量は、通
常、使用単量体100重量部当り、0.05〜5重量
部、好ましくは0.2〜4重量部の範囲で適宜選択する
ことができる。In carrying out the fine suspension polymerization method, usually,
Surfactants and dispersants are used. Examples of the surfactant include alkyl sulfates such as sodium lauryl sulfate and sodium myristyl sulfate; alkyls such as sodium dodecylbenzenesulfonate and potassium dodecylbenzenesulfonate. Aryl sulfonates; sulfosuccinates such as sodium dioctyl sulfosuccinate and sodium dihexyl sulfosuccinate; fatty acid salts such as ammonium laurate and potassium stearate; polyoxyethylene alkyl sulfates; polyoxyethylene alkyl aryl sulfates; Further, anionic surfactants such as sodium dodecyl diphenyl ether disulfonate; sorbitan monooleate, polyoxyethylene sorbita; Sorbitan esters such as monostearate; polyoxyethylene alkyl ethers; nonionic surfactants such as polyoxyethylene alkyl phenyl ethers; cetylpyridinium chloride,
Cationic surfactants such as cetyltrimethylammonium bromide can be mentioned. Further, as a dispersant, polyvinyl alcohol, methyl cellulose,
Polyvinylpyrrolidone and the like can be mentioned. These surfactants and dispersants may be used alone or in combination with two or more.
A combination of more than one species may be used. The amount used can be appropriately selected usually from 0.05 to 5 parts by weight, preferably from 0.2 to 4 parts by weight, per 100 parts by weight of the monomer used.
【0028】また、該微細懸濁重合法では、まず水性媒
体中に、油溶性開始剤、単量体、界面活性剤及び必要に
応じて用いられる高級脂肪酸類や高級アルコール類など
の重合助剤その他の添加剤を加えて予め混合し、ホモジ
ナイザーにより均質化処理して、油滴の粒径調節を行な
う。ホモジナイザーには、例えば、コロイドミル、振動
撹拌機、二段式高圧ポンプ、ノズルやオリフィス等から
の高圧噴出、超音波撹拌等が利用できる。加えて、油滴
粒径の調節は、均質化処理時の剪断力の制御、重合中の
撹拌条件、反応装置の形式、界面活性剤や添加剤の量等
に影響されるが、これらは、簡単な予備実験により適当
な条件を選択することができる。そして、全単量体の均
質化処理液を重合缶に送り、ゆっくりと撹拌しながら昇
温し、通常30〜80℃の範囲の温度において重合を行
なう。In the fine suspension polymerization method, first, an oil-soluble initiator, a monomer, a surfactant and, if necessary, a polymerization aid such as a higher fatty acid or a higher alcohol in an aqueous medium. Other additives are added and mixed in advance, and homogenized by a homogenizer to adjust the particle diameter of oil droplets. As the homogenizer, for example, a colloid mill, a vibration stirrer, a two-stage high-pressure pump, high-pressure ejection from a nozzle or an orifice, ultrasonic stirring, or the like can be used. In addition, the adjustment of the oil droplet size is affected by the control of the shear force during the homogenization treatment, the stirring conditions during the polymerization, the type of the reactor, the amount of the surfactant and the additives, etc. Appropriate conditions can be selected by simple preliminary experiments. Then, the homogenized solution of all the monomers is sent to a polymerization vessel, and the temperature is increased while stirring slowly, and polymerization is usually performed at a temperature in the range of 30 to 80 ° C.
【0029】このようにして一次平均粒径が0.03〜
5.0μmの熱可塑性樹脂粉末の粒子が均質に分散した
乳化液または懸濁液を得ることができる。この乳化液又
は懸濁液を噴霧乾燥したり、あるいは、熱可塑性樹脂の
粒子を凝集した後に、ろ過して液漿を分離し、乾燥、粉
砕することで熱可塑性樹脂粉末を得ることができる。そ
の熱可塑性樹脂の重量平均分子量は、反応温度や重合度
調節剤で所望の値に調節すれば良い。In this way, the primary average particle size is from 0.03 to
An emulsion or suspension in which particles of a 5.0 μm thermoplastic resin powder are homogeneously dispersed can be obtained. The emulsion or suspension is spray-dried, or the particles of the thermoplastic resin are agglomerated, then filtered to separate the plasma, dried and pulverized to obtain a thermoplastic resin powder. The weight average molecular weight of the thermoplastic resin may be adjusted to a desired value with a reaction temperature or a polymerization degree regulator.
【0030】本発明では、前記した混合物に加え、合金
用粉末や切削性改善用粉末の偏析防止効果に優れた混合
物をも提供している。それは、鉄基粉末と、該鉄基粉末
に溶融・付着したステアリン酸、オレイン酸アミド、ス
テアリン酸アミド、ステアリン酸アミドとエチレンビス
ステアリン酸アミドとの溶融混合物、エチレンビスステ
アリン酸アミドの内から選ばれた1種以上の潤滑剤0.
1重量%以上1.0重量%以下と、前記潤滑剤により前
記鉄基粉末に付着した合金用粉末及び/又は切削性改善
用粉末と、少なくとも前記アクリル酸エステル、メタク
リル酸エステル及び芳香族ビニル化合物の中から選ばれ
た1種の単量体単位を50%以上含有する熱可塑性樹脂
の粉末を0.05重量%以上0.50重量%以下を含有
し、さらに必要に応じてステアリン酸、オレイン酸アミ
ド、ステアリン酸アミド、ステアリン酸アミドとエチレ
ンビスステアリン酸アミドとの溶融混合物、エチレンビ
スステアリン酸アミド、分子量1万以下のポリエチレ
ン、エチレンビスステアリン酸アミドと分子量1万以下
ポリエチレンとの溶融混合物からなる群から選ばれた1
種以上の潤滑剤を0.50重量%以下を含む遊離粉末と
を配合したものである。これにより、ステアリン酸亜鉛
のような金属石鹸を潤滑剤として用いなくとも、合金用
粉末等の混合物中での偏析が防止されるばかりでなく、
従来品並みの粉体及び圧粉体の特性が十分に維持され、
流動性やホッパ排出性に優れたものになるからである。
偏析が防止されるのは、鉄基粉末に付着した潤滑剤が結
合作用を発揮し、合金用粉末及び/又は切削性改善用粉
末を鉄基粉末表面に固着させるからである。In the present invention, in addition to the above-mentioned mixture, there is also provided a mixture having an excellent segregation preventing effect of alloy powder or machinability improving powder. It is selected from iron-based powder, stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylene bis-stearic acid amide, and ethylene bis-stearic acid amide fused and adhered to the iron-based powder. One or more lubricants
1% by weight or more and 1.0% by weight or less, an alloy powder and / or a machinability improving powder adhered to the iron-based powder by the lubricant, and at least the acrylic ester, methacrylic ester and aromatic vinyl compound Containing 0.05% to 0.50% by weight of a thermoplastic resin powder containing 50% or more of one type of monomer unit selected from the group consisting of stearic acid and olein, if necessary. Acid amide, stearic acid amide, molten mixture of stearic acid amide and ethylene bis stearic acid amide, ethylene bis stearic acid amide, polyethylene having a molecular weight of 10,000 or less, molten mixture of ethylene bis stearic amide and polyethylene having a molecular weight of 10,000 or less 1 selected from the group
It contains a free powder containing 0.50% by weight or less of at least one kind of lubricant. Thereby, without using a metal soap such as zinc stearate as a lubricant, not only segregation in a mixture such as alloy powder is prevented, but also
The characteristics of the powder and the green compact comparable to conventional products are sufficiently maintained,
This is because the fluidity and the hopper discharge property are excellent.
The reason why segregation is prevented is that the lubricant attached to the iron-based powder exerts a binding action and fixes the alloy powder and / or the machinability improving powder to the iron-based powder surface.
【0031】また、本発明では、結合作用を発揮する潤
滑剤を用いずに、鉄基粉末と、合金用粉末及び/又は切
削性改善粉末と、前記と同一の潤滑剤からなる群から選
ばれた1種以上0.1重量%以上1.0重量%以下の遊
離粉末と、前記所定のアクリル酸エステル、メタクリル
酸エステル及び芳香族ビニル化合物の中から選ばれた少
なくとも1種の単量体単位を50%以上含有する熱可塑
性樹脂の0.05重量%以上0.50重量%以下の遊離
粉末とを単純に混合することで、従来品並みの粉体及び
圧粉体の特性を十分に維持し、流動性やホッパ排出性に
優れた鉄基粉末混合物(以下、単純混合粉末ということ
あり)をも提供している。次に、本発明に係る混合物の
製造方法であるが、それは、以下の工程で順次行われ
る。Further, in the present invention, without using a lubricant exhibiting a binding action, it is selected from the group consisting of iron-based powder, powder for alloying and / or powder for improving machinability, and the same lubricant as described above. And at least one monomer unit selected from the above-mentioned predetermined acrylate, methacrylate and aromatic vinyl compounds. Of a thermoplastic resin containing at least 50% by weight and a free powder of at least 0.05% by weight and at most 0.50% by weight, to thereby sufficiently maintain the properties of powder and green compact comparable to conventional products. Further, the present invention also provides an iron-based powder mixture (hereinafter, sometimes referred to as a simple mixed powder) having excellent fluidity and hopper dischargeability. Next, a method for producing a mixture according to the present invention is performed sequentially in the following steps.
【0032】(1) 下記の潤滑剤の群から選ばれた1
種以上を0.1重量%以上 1.0重量%以下と、合金
用粉末及び/又は切削性改善用粉末と、鉄基粉末とを混
合する。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミド (2) その混合物を、潤滑剤が1種の場合は、その融
点のプラス10〜100℃で、潤滑剤が2種以上からな
る場合は、それら融点のうちの最低の融点プラス10℃
以上、最高の融点以下の温度で、加熱しながら混合し、
少なくとも1種以上の潤滑剤を溶融させる。 (3) 該混合物を冷却して、鉄基粉末の表面に合金用
粉末及び/又は切削性改善用粉末を強固に付着させる。 (4) その後、前記有機潤滑剤の最低の融点未満、好
ましくは室温で前記所定のアクリル酸エステル、メタク
リル酸エステル及び芳香族ビニル化合物の中から選ばれ
た少なくとも1種の単量体単位を50%以上含有する熱
可塑性粉末0.05重量%以上0.50重量%以下とを
添加、混合する。 (5) さらに必要に応じて、下記の潤滑剤群から選ば
れた1種以上の潤滑剤の粉末0.50重量%以下を添
加、混合する。 記 ステアリン酸(融点69℃)、オレイン酸アミド(融点
76℃)、ステアリン酸アミド(融点103℃)、ステ
アリン酸アミドとエチレンビスステアリン酸アミドとの
溶融混合物(融点125℃)、エチレンビスステアリン
酸アミド(融点147℃)、分子量1万以下のポリエチ
レン(融点110〜150℃)、エチレンビスステアリ
ン酸アミドと分子量1万以下のポリエチレンの溶融混合
物(130〜140℃)。(1) 1 selected from the following lubricant group
0.1% by weight or more and 1.0% by weight or less of the seed or more, the alloy powder and / or the machinability improving powder, and the iron-based powder are mixed. Note: Stearic acid, oleic acid amide, stearic acid amide, molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide (2) In the case of plus 10 to 100 ° C. and two or more lubricants, the lowest melting point among those melting points plus 10 ° C.
Above, at a temperature below the highest melting point, mixing while heating,
At least one or more lubricants are melted. (3) The mixture is cooled, and the alloy powder and / or the machinability improving powder are firmly adhered to the surface of the iron-based powder. (4) Thereafter, at least less than the minimum melting point of the organic lubricant, preferably at room temperature, at least one monomer unit selected from the above-mentioned predetermined acrylic ester, methacrylic ester and aromatic vinyl compound is used. % Of thermoplastic powder containing 0.05% by weight or more and 0.50% by weight or less. (5) Further, if necessary, 0.50% by weight or less of powder of one or more lubricants selected from the following lubricant group is added and mixed. Stearic acid (melting point 69 ° C.), oleic acid amide (melting point 76 ° C.), stearic acid amide (melting point 103 ° C.), molten mixture of stearic acid amide and ethylenebisstearic acid amide (melting point 125 ° C.), ethylenebisstearic acid Amide (melting point: 147 ° C), polyethylene having a molecular weight of 10,000 or less (melting point: 110 to 150 ° C), melt mixture of ethylenebisstearic acid amide and polyethylene having a molecular weight of 10,000 or less (130 to 140 ° C).
【0033】これらの潤滑剤を用いるのは、従来用いて
いた金属元素を含むステアリン酸亜鉛(融点120℃)
と同様に、この鉄基粉末混合物を金型中で加圧成形する
際、摩擦熱で溶融ないし軟化させて、本来の潤滑剤の働
きをさせるためである。加熱溶融混合により、合金用粉
末及び/又は切削性改善用粉末の鉄基粉末への付着度は
向上する。加熱溶融させ、結合作用を発揮する潤滑剤の
量が、0.1重量%未満では、合金用粉末等の鉄基粉末
表面への付着量が低下し、混合物中でのその偏析が増加
する。該潤滑剤の量が1.0重量%を超えて多くなり過
ぎると、ホッパ排出性を向上させることができない。These lubricants are used because zinc stearate containing a metal element which has been conventionally used (melting point: 120 ° C.)
Similarly to the above, when the iron-based powder mixture is pressed and molded in a mold, the mixture is melted or softened by frictional heat to work as an original lubricant. The degree of adhesion of the alloy powder and / or the machinability improving powder to the iron-based powder is improved by the heat melting and mixing. If the amount of the lubricant which is heated and melted and exerts the binding action is less than 0.1% by weight, the amount of the lubricant adhered to the surface of the iron-based powder such as alloy powder is reduced, and the segregation in the mixture is increased. If the amount of the lubricant exceeds 1.0% by weight, the hopper discharge property cannot be improved.
【0034】また、前記(5)の工程において、常温
で、(5)に記載されたものと同一の潤滑剤からなる群
から選ばれた1種以上の粉末0.50重量%以下を添加
するのは、前述のように、金型中で加圧成形する際、摩
擦熱で溶融ないし軟化して潤滑剤の働きをさせるためで
ある。0.50重量%を超えて添加すると、ホッパから
円滑に排出させることができなくなる。In the step (5), at room temperature, 0.50% by weight or less of one or more powders selected from the group consisting of the same lubricants as described in (5) is added. This is because, as described above, when pressure molding is performed in a mold, the lubricant is melted or softened by frictional heat to function as a lubricant. If it is added in excess of 0.50% by weight, it cannot be discharged smoothly from the hopper.
【0035】さらに、本発明に係る混合物には、オレイ
ン酸、スピンドル油、タービン油から選ばれた1種以上
の有機質液体潤滑剤0.01重量%以上、0.3重量%
以下が、前記潤滑剤と共に添加されることがある。それ
により、合金用粉末等の鉄基粉末への付着が強固になる
と共に、混合物自体の見掛密度値が安定するからであ
る。その添加量は、0.01重量%未満では、見掛密度
値を安定させる作用がなく、0.3重量%を超えると、
ホッパ排出性が低下する。また、これら液体潤滑剤の添
加時期は、鉄基粉末(鉄粉)と他の添加物(合金粉末
等)とを混合する前が好ましい。その理由は、液体潤滑
剤は、鉄粉と他の添加物との撹拌混合時にすみやかに鉄
粉表面を覆い、撹拌に起因して生じる鉄粉粒子の表面摩
擦、衝突による変形を抑制し、この変形によるホッパ排
出性低下を抑制すると共に、鉄粉表面への添加物の均一
付着を容易にする作用も有するためである。混合中に添
加するのでは、前記見掛密度値の安定化作用が小さく、
ホッパ排出性も低下し、さらに混合後に添加するので
は、見掛密度値の安定化作用、ホッパ排出性共に低下す
る。この液体潤滑剤を用いる場合も、加熱溶融混合によ
って結合作用を発揮する前記有機潤滑剤の添加量は、液
体潤滑剤を用いない場合と同等で良い。Further, the mixture according to the present invention contains at least 0.01% by weight and at least 0.3% by weight of one or more organic liquid lubricants selected from oleic acid, spindle oil and turbine oil.
The following may be added with the lubricant: Thereby, the adhesion of the alloy powder to the iron-based powder becomes strong, and the apparent density value of the mixture itself is stabilized. When the amount of addition is less than 0.01% by weight, there is no effect of stabilizing the apparent density value, and when it exceeds 0.3% by weight,
Hopper discharge is reduced. It is preferable to add these liquid lubricants before mixing the iron-based powder (iron powder) with other additives (such as alloy powder). The reason is that the liquid lubricant quickly covers the surface of the iron powder during stirring and mixing of the iron powder and other additives, suppresses surface friction of the iron powder particles caused by stirring, deformation due to collision, This is because it has a function of suppressing a decrease in the hopper discharge property due to the deformation and facilitating uniform attachment of the additive to the surface of the iron powder. By adding during mixing, the effect of stabilizing the apparent density value is small,
The hopper discharge property also decreases, and if added after mixing, both the effect of stabilizing the apparent density value and the hopper discharge property decrease. Also in the case of using this liquid lubricant, the amount of the organic lubricant that exerts the binding action by heating and melting and mixing may be equivalent to the case where no liquid lubricant is used.
【0036】さらに、本発明では、前記加熱温度は、用
いられる潤滑剤(液体潤滑剤を除く潤滑剤)が1種の場
合は、その融点プラス10℃以上100℃以下に、2種
以上の場合は、最低融点の潤滑剤の融点プラス10℃以
上、最高融点の潤滑剤の融点以下とする。潤滑剤が1種
の場合は、融点プラス10℃以上の加熱で溶融せしめ、
結合機能を発揮させ、融点プラス100℃以下とするこ
とで、潤滑剤の熱分解による結合機能の低下が防止でき
るからである。潤滑剤が2種以上の場合は、そのうちの
最低融点の潤滑剤の融点プラス10℃以上で少なくとも
1種以上の潤滑剤を溶融して結合機能を発揮させ、最高
融点の潤滑剤の融点以下とすることで、熱分解による機
能低下を防止すると共に、ホッパ排出性能を向上させ
る。Further, in the present invention, the heating temperature is set to the melting point plus 10 ° C. or more and 100 ° C. or less when one kind of lubricant (lubricant excluding liquid lubricant) is used. Is equal to or higher than the melting point of the lubricant having the lowest melting point plus 10 ° C. and equal to or lower than the melting point of the lubricant having the highest melting point. In the case of one kind of lubricant, it is melted by heating at the melting point plus 10 ° C or more,
By exhibiting the bonding function and setting the melting point to 100 ° C. or lower, it is possible to prevent the deterioration of the bonding function due to the thermal decomposition of the lubricant. When two or more lubricants are used, at least one of the lubricants is melted at a temperature higher than the melting point of the lubricant having the lowest melting point plus 10 ° C. or more to exhibit a bonding function, and the melting point of the lubricant having the highest melting point is lower than the melting point of the lubricant having the highest melting point. By doing so, it is possible to prevent functional deterioration due to thermal decomposition and to improve hopper discharge performance.
【0037】一方、単純混合粉末の製造においては、下
記の潤滑剤の群から選ばれた1種以上を0.1重量%以
上1.0重量%以下と、前記所定のアクリル酸エステ
ル、メタクリル酸エステル及び芳香族ビニル化合物の中
から選ばれた少なくとも1種の単量体単位を50%以上
含有する熱可塑性樹脂粉末0.05重量%以上0.50
重量%以下とを遊離粉末の潤滑剤として、鉄基粉末、合
金粉末、切削性改善用粉末等に単純に添加、混合する。
これだけで、従来の粉体特性、および圧粉体特性を十分
に維持し、流動性やホッパ排出性に優れた鉄基混合粉末
が得られるからである。下記潤滑剤の群から選ばれた1
種以上を0.1重量%以上1.0重量%以下とするの
は、0.1重量%未満では、金型からの成形体の抜出力
(以下、単に抜出力という)が高くなり過ぎ、1.0重
量%を超えると、流動性が低下するためである。また、
アクリル酸エステル、メタクリル酸エステル及び芳香族
ビニル化合物の中から選ばれた少なくとも1種の単量体
単位を50%以上含有する熱可塑性微粉末の添加量を
0.05%重量%以上0.50重量%以下に添加するの
は、添加量が0.05%重量%未満では、ホッパ排出性
が低下するためであり、0.5重量%を超えると、圧縮
性が低下するからである。さらに、熱可塑性樹脂の微粉
末の形状を一次粒子径が0.03μm以上5μm以下
で、凝集平均径が5〜50μmと規定するのは、前記と
同一理由による。なお、混合には、V型ブレンダーやW
型コーンミキサー等を利用するのが好ましい。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドの溶融化合物、エチレンビスステアリン酸アミド、
分子量1万以下のポリエチレン、エチレンビスステアリ
ン酸アミドと分子量1万以下のポリエチレン溶融混合
物。On the other hand, in the production of the simple mixed powder, at least one selected from the group consisting of the following lubricants is used in an amount of 0.1% by weight or more and 1.0% by weight or less, and 0.05% by weight or more and 0.50% by weight or more of thermoplastic resin powder containing 50% or more of at least one monomer unit selected from esters and aromatic vinyl compounds.
% By weight or less as a lubricant of a free powder is simply added to and mixed with an iron-based powder, an alloy powder, a powder for improving machinability, and the like.
This is because the iron-based mixed powder having sufficient fluidity and hopper discharge property can be obtained by sufficiently maintaining the conventional powder properties and green compact properties. 1 selected from the group of the following lubricants
When the amount of the seeds is set to 0.1% by weight or more and 1.0% by weight or less, if it is less than 0.1% by weight, the ejection force (hereinafter, simply referred to as ejection force) of the molded article from the mold becomes too high. If the content exceeds 1.0% by weight, the fluidity decreases. Also,
The addition amount of the thermoplastic fine powder containing 50% or more of at least one monomer unit selected from acrylates, methacrylates and aromatic vinyl compounds is 0.05% by weight to 0.50% by weight. The reason why it is added in an amount of not more than 0.05% by weight is that if the amount is less than 0.05% by weight, the hopper discharge property is reduced, and if it is more than 0.5% by weight, the compressibility is reduced. Further, the reason that the shape of the fine powder of the thermoplastic resin is specified to have a primary particle diameter of 0.03 μm or more and 5 μm or less and an average agglomeration diameter of 5 to 50 μm is the same as above. In addition, V type blender or W
It is preferable to use a mold cone mixer or the like. Note stearic acid, oleic acid amide, stearic acid amide, a molten compound of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide,
Polyethylene having a molecular weight of 10,000 or less, ethylene bisstearic acid amide and a polyethylene melt mixture having a molecular weight of 10,000 or less.
【0038】[0038]
【実施例】表1に、本発明の実施例で使用した熱可塑性
樹脂粉末の種類と、それらの組成及び重合方法を示して
おく。また、実施例は、偏析防止を重視した混合物に関
する(A)グループと、前記単純混合物に関する(B)
グループに大別して行った。EXAMPLES Table 1 shows the types of thermoplastic resin powders used in the examples of the present invention, their compositions and polymerization methods. Further, in the examples, the group (A) relating to the mixture with emphasis on segregation prevention and the group (B) relating to the simple mixture are described.
We went into groups.
【0039】[0039]
【表1】 [Table 1]
【0040】(Aグループ)本発明に係る粉末冶金用粉
末混合物を製造するため、まず、平均粒径78μmの鉄
粉(鉄基粉末)に、平均粒径23μmの黒鉛粉末(合金
用粉末)1重量%と、平均粒径25μmの電解銅粉(合
金用粉末)を2重量%と、表2に示す1次混合した潤滑
剤(有機潤滑剤及び液体潤滑剤)とを、加熱混合機に装
入して十分に混合した。そして、混合した前記の有機潤
滑剤の最低融点+10℃以上、最高融点以下の温度で、
混合を続けながら加熱した(ここまでを1次混合とい
う)。引き続き、混合しながら、該混合物を85℃以下
に冷却した。さらに、40℃まで冷却した後、遊離粉末
として表3に示す二次混合した潤滑剤、すなわち潤滑剤
(ロ)及び/又は熱可塑性樹脂粉末を添加し、均一にな
るよう混合し(2次混合という)、該加熱混合機から排
出した。(Group A) In order to manufacture the powder mixture for powder metallurgy according to the present invention, first, graphite powder (alloy powder) having an average particle diameter of 23 μm was added to iron powder (iron-based powder) having an average particle diameter of 78 μm. % By weight, 2% by weight of electrolytic copper powder (powder for alloy) having an average particle size of 25 μm, and a primary-mixed lubricant (organic lubricant and liquid lubricant) shown in Table 2 were mounted on a heating mixer. And mixed well. Then, at a temperature not lower than the lowest melting point of the mixed organic lubricant + 10 ° C. and not higher than the highest melting point,
The mixture was heated while continuing to mix (this is called primary mixing). Subsequently, the mixture was cooled to 85 ° C. or lower while mixing. Further, after cooling to 40 ° C., a secondary-mixed lubricant shown in Table 3 as a free powder, that is, a lubricant (b) and / or a thermoplastic resin powder is added and mixed so as to be uniform (secondary mixing). ) And discharged from the heating mixer.
【0041】[0041]
【表2】 [Table 2]
【0042】[0042]
【表3】 [Table 3]
【0043】一方、上記のようにして製造した本発明に
係る混合物と特性を比較するため、使用粉末を同一に
し、潤滑剤の配合や製造条件を表5及び表6のように変
更して、別途に混合物を製造した(以下、比較例とい
う)。On the other hand, in order to compare the properties with the mixture according to the present invention produced as described above, the powder used was the same, and the blending of the lubricant and the production conditions were changed as shown in Tables 5 and 6. A mixture was separately manufactured (hereinafter, referred to as a comparative example).
【0044】[0044]
【表5】 [Table 5]
【0045】[0045]
【表6】 [Table 6]
【0046】なお、本明細書に記載する全ての表では、
本発明に係る実施例を、Aグループのものは記号A実1
〜43、Bグループのものは記号B実44〜77で表わ
し、比較例をAグループのものはA比1〜14、Bグル
ープのものはB比15〜26で表わす。In all the tables described in this specification,
In the embodiment according to the present invention, those of the group A are denoted by the symbol A
4343 and B group are represented by symbols B-444477, and the comparative examples are represented by A ratio 11〜14 for group A and B ratio 15〜26 for group B.
【0047】次に、これらの混合物を金型に充填し、成
形体として直径25mm、高さ20mmのタブレットに
5t/cm2の圧力で成形した。表4に、本発明に係る
混合粉で製作した前記成形体の抜出力と、混合物100
gをオリフィス径5mmの容器に充填してから排出する
までの時間で、該混合物の流動性の値を示した。また、
この混合物のホッパ排出性は、内径100mm、高さ2
00mmの容器の底部中央に設けた直径2.0mmのオ
リフィスを通して、該混合物1000gを全て排出させ
るまでの加振回数で評価した。さらに、上記成形体の成
形密度を測定した後、RXガスの雰囲気中で1130℃
で20分間焼結し、その焼結体の表面に煤があるか否か
を目視で判断した結果も、表4に示した。前記測定した
成形体の成形密度は、混合物の圧縮性評価の指標とし
た。一方、混合物を成形密度6.8Mg/m3の成形体
に成形した後、該成形体を上述した条件で焼結し、焼結
体の引張強さを測定した。また、混合物に含まれる黒鉛
粉の偏析程度を示す尺度として、炭素Cの付着度も評価
した。その付着度は、混合粉末の篩分けと炭素の定量分
析を行った結果を、次式で表わすようにした。この値が
大きい程、混合粉末での黒鉛粉の偏析が小さいことを意
味する。Next, the mixture was filled in a mold, and molded into a tablet having a diameter of 25 mm and a height of 20 mm as a molded body at a pressure of 5 t / cm 2. Table 4 shows the ejection force of the molded body manufactured using the mixed powder according to the present invention and the mixture 100
The value of the fluidity of the mixture was indicated by the time from when g was filled into a container having an orifice diameter of 5 mm until the container was discharged. Also,
The hopper discharge property of this mixture is 100 mm in inner diameter and 2 mm in height.
The evaluation was performed by the number of times of vibration until 1000 g of the mixture was completely discharged through an orifice having a diameter of 2.0 mm provided at the center of the bottom of a 00 mm container. Further, after measuring the molding density of the molded body, the molded body was heated at 1130 ° C. in an atmosphere of RX gas.
Table 4 also shows the results of visually determining whether or not soot was present on the surface of the sintered body. The measured compacting density of the compact was used as an index for evaluating the compressibility of the mixture. On the other hand, after the mixture was molded into a molded body having a molding density of 6.8 Mg / m3, the molded body was sintered under the conditions described above, and the tensile strength of the sintered body was measured. Further, as a scale indicating the degree of segregation of the graphite powder contained in the mixture, the degree of adhesion of carbon C was also evaluated. The degree of adhesion was determined by sieving the mixed powder and performing quantitative analysis of carbon by the following equation. The larger the value, the smaller the segregation of the graphite powder in the mixed powder.
【0048】炭素Cの付着度=(100メッシュ(15
0μm)を通過したものから200メッシュ(75μ
m)を通過しない範囲の粒度までの鉄基混合粉のC分析
値)/(鉄基混合粉のC分析値)×100(%)Degree of adhesion of carbon C = (100 mesh (15
0 μm) and 200 mesh (75 μm)
m) C analysis value of iron-based mixed powder up to a particle size not passing through m) / (C analysis value of iron-based mixed powder) × 100 (%)
【0049】[0049]
【表4】 [Table 4]
【0050】表4のA実1からA実43までに示すよう
に、本発明に係る粉末や潤滑剤の配合で鉄基粉末混合物
を製造すれば、潤滑剤に金属元素を含むステアリン酸亜
鉛やステアリン酸リチウムを使用しなくとも、流動性が
10.1/100g〜11.9秒/100gで、ホッパ
排出性1〜2回と優れ、抜出力が115〜129kgf
/cm2と低く、焼結体に煤の付着も見られず、Cの付
着率が80〜91%の粉末冶金用鉄基粉末混合物とする
ことができる。一方、後述するように、比較例はいずれ
かの特性が劣る。As shown in Tables A-A1 to A-A43, if an iron-based powder mixture is produced by mixing the powder and the lubricant according to the present invention, zinc stearate containing a metal element in the lubricant can be used. Even if lithium stearate is not used, the fluidity is 10.1 / 100 g to 11.9 seconds / 100 g, the hopper discharge property is excellent once or twice, and the ejection force is 115 to 129 kgf.
/ Cm 2, soot is not observed on the sintered body, and an iron-based powder mixture for powder metallurgy having an adhesion ratio of C of 80 to 91% can be obtained. On the other hand, as described below, the comparative example is inferior in any of the characteristics.
【0051】比較例としての条件で製造した混合物につ
いても、実施例と同様の評価を行い、結果を表7に整理
した。表7より、A比1の混合物は、熱可塑性樹脂粉末
の平均分子量が500万を超えているため、A比3及び
4の混合物は、熱可塑性樹脂粉末の凝集平均粒径が5μ
m未満のため、混合物の流動性とホッパ排出性が低いこ
とが明らかである。また、熱可塑性樹脂粉末の一次平均
粒径が5μmを超えているA比2の混合物は、該樹脂粉
末以外の潤滑剤配合が同じであるA実2の混合物と比較
して、混合物の圧縮性が0.15Mg/m3低下した。
さらに、A比5の混合物は、熱可塑性樹脂粉末の凝集平
均粒径が50μmを超えているので、それによって製造
した焼結体の引張り強さは、A実1〜43の混合物によ
る焼結体の引張強さ410から440MPaに対し、3
60MPaと低かった。A比6の混合物は、熱可塑性樹
脂粉末の配合量が少なく、流動性とホッパ排出性が低下
した。そして、A比7の混合物は、熱可塑性樹脂粉末の
配合量が0.5重量%を超えているため、A比7の混合
物に対して、熱可塑性樹脂粉末以外は同じ潤滑剤を配合
したA実2の混合物と比較し、圧縮性が0.07Mg/
m3だけ低い。A比8の混合物は、加熱混合される潤滑
剤量が1重量%を超えているので、流動性、ホッパ排出
性が悪く、A比9の混合物は、加熱混合される潤滑剤料
が0.1重量%未満で、C付着量が低い。A比10の混
合物は、2次混合で添加される熱可塑性樹脂以外の潤滑
剤の配合が多く、A比11及び12は、結合剤としての
液体潤滑剤の配合が多く、製造した混合物の流動性、ホ
ッパ排出性が悪い。The same evaluations as in the examples were carried out for the mixtures produced under the conditions as comparative examples, and the results are shown in Table 7. From Table 7, since the mixture of A ratio 1 has an average molecular weight of the thermoplastic resin powder exceeding 5,000,000, the mixture of A ratios 3 and 4 has a coagulation average particle size of the thermoplastic resin powder of 5 μm.
It is clear that the fluidity of the mixture and the hopper discharge are low because it is less than m. Further, the mixture having a ratio A of 2 in which the average primary particle size of the thermoplastic resin powder exceeds 5 μm has a compressibility of the mixture which is lower than that of the mixture of the solid A2 having the same lubricant composition other than the resin powder. Decreased by 0.15 Mg / m3.
Furthermore, since the mixture having an A ratio of 5 has a thermoplastic resin powder having an agglomeration average particle size of more than 50 μm, the tensile strength of the sintered body produced therefrom is as follows: For tensile strength of 410 to 440 MPa, 3
It was as low as 60 MPa. In the mixture having the A ratio of 6, the blending amount of the thermoplastic resin powder was small, and the fluidity and the hopper discharge property were reduced. Since the blending amount of the thermoplastic resin powder in the mixture of A ratio 7 exceeds 0.5% by weight, the same lubricant as that of the mixture of A ratio 7 except for the thermoplastic resin powder is blended with the mixture of A ratio 7. The compressibility is 0.07 Mg /
m3 lower. The mixture with the A ratio of 8 has a poor fluidity and hopper discharge property because the amount of the lubricant to be heated and mixed exceeds 1% by weight. At less than 1% by weight, the C adhesion amount is low. The mixture having an A ratio of 10 contains a large amount of a lubricant other than the thermoplastic resin added in the secondary mixing, and the A ratios of 11 and 12 contain a large amount of a liquid lubricant as a binder. And hopper discharge property are poor.
【0052】なお、上記比較例及び実施例で製造した焼
結体には、いずれも煤の発生が見られなかった。また、
金型からの成形体の抜出力も、実施例と比較例とで差が
なかった。It should be noted that no soot was generated in any of the sintered bodies manufactured in the comparative example and the example. Also,
The output of the molded product from the mold was not different between the example and the comparative example.
【0053】[0053]
【表7】 [Table 7]
【0054】(Bグループ)平均粒径78μmの粉末冶
金用鉄粉(鉄基粉末)に、平均粒径23μmの黒鉛粉末
(合金用粉末)1重量%と、平均粒径25μmの銅粉末
(合金用粉末)1重量%と表8に示す潤滑剤(ハ)と熱
可塑性樹脂粉末とを、V型ブレンダーで15分間単純に
混合し、混合物とした。また、上記同様に潤滑剤(ハ)
と熱可塑性樹脂粉末とを表11のようにして、比較例と
しての混合物も製造した。これらの混合物の評価は、前
記Aグループに属するものと同じ方法で行ない、表9及
び表10の結果を得た。(Group B) 1% by weight of graphite powder (alloy powder) having an average particle diameter of 23 μm and copper powder (alloy powder) having an average particle diameter of 25 μm were added to iron powder for powder metallurgy (iron-based powder) having an average particle diameter of 78 μm. Powder for use), 1% by weight of the lubricant (c) shown in Table 8, and the thermoplastic resin powder were simply mixed in a V-type blender for 15 minutes to obtain a mixture. Also, as described above, the lubricant (c)
And a thermoplastic resin powder, as shown in Table 11, a mixture as a comparative example was also produced. Evaluation of these mixtures was performed in the same manner as in the group A, and the results in Tables 9 and 10 were obtained.
【0055】[0055]
【表8】 [Table 8]
【0056】[0056]
【表11】 [Table 11]
【0057】表9の実施例B実44からB実77までに
示すように、本発明に係る混合物は、潤滑剤に金属元素
を含むステアリン酸亜鉛やステアリン酸リチウムを使用
しなくとも、流動性が12.0〜12.7秒/100
g、ホッパ排出性(1回以下)に優れ、抜出力が112
〜128kgf/cm2と低く、また圧縮性、焼結体の
引張強さ、焼結体に煤が付着していないこと等、全ての
特性に問題のない粉末冶金用鉄基粉末混合物となる。一
方、後述べるように、比較例はいずれかの特性値が劣
る。As shown in Examples B-44 to B-77 in Table 9, the mixture according to the present invention has a high fluidity without using zinc stearate or lithium stearate containing a metal element as a lubricant. Is 12.0-12.7 seconds / 100
g, excellent hopper discharge (1 time or less), and withdrawal power of 112
It is as low as ~ 128 kgf / cm2, and the iron-based powder mixture for powder metallurgy has no problem in all properties such as compressibility, tensile strength of the sintered body, and no soot adhered to the sintered body. On the other hand, as described later, the comparative example is inferior in any of the characteristic values.
【0058】[0058]
【表9】 [Table 9]
【0059】[0059]
【表10】 [Table 10]
【0060】B比13、14及び15の混合物は、それ
ぞれステアリン酸アミド、ステアリン酸アミドとエチレ
ンビスステアリン酸アミドとの溶融混合物、エチレンビ
スステアリン酸アミドを単独で潤滑剤として単純混合し
たが、流動性、ホッパ排出性に劣っている。また、B比
16の混合物は、熱可塑性樹脂粉末の配合量が0.5重
量%を超えているので、その配合量以外は同じ潤滑剤を
配合したB実52の混合物と比較すると、圧縮性が0.
07Mg/m3だけ低下している。B比17の混合物
は、熱可塑性樹脂粉末の平均分子量が500万を超えて
いるため、B比19及び20の混合物は、熱可塑性樹脂
粉末の凝集平均粒径が5μm未満のため、流動性とホッ
パ排出性が低い。さらに、B比18の混合物は、熱可塑
性樹脂粉末の一次粒径が5μmを超えているので、それ
以外は同じ潤滑剤の配合のB実49と比較すると、圧縮
性が0.15Mg/m3だけ低い。B比21は、熱可塑
性樹脂粉末の凝集平均径が50μmを超えているので、
すべてのB実44〜77の混合物では引張強さが400
から440MPaであったのに対し、B比21の混合物
では、370MPaに低下した。また、B比22の混合
物は、熱可塑性樹脂粉末以外の潤滑剤の合計量添加量が
0.1重量%未満で、抜出力が高く、B比23の混合物
は、前記潤滑剤の合計添加量が1重量%を超えているの
で、流動性、ホッパ排出性が悪い。Mixtures having a B ratio of 13, 14 and 15 were prepared by mixing stearic acid amide, a molten mixture of stearic acid amide and ethylene bis stearic acid amide, and ethylene bis stearic acid amide alone as a lubricant. And hopper discharge property. In addition, since the blending ratio of the thermoplastic resin powder of the mixture having a B ratio of 16 exceeds 0.5% by weight, the mixture having a compressibility of less than that of the blend of B-B52 mixed with the same lubricant except for the blending amount is used. Is 0.
It has decreased by 07 Mg / m3. The mixture having a B ratio of 17 has a thermoplastic resin powder having an average molecular weight of more than 5,000,000, and the mixture having a B ratio of 19 or 20 has a fluidity of less than 5 μm because the thermoplastic resin powder has an aggregation average particle size of less than 5 μm. Low hopper discharge. Furthermore, since the mixture having a B ratio of 18 has a thermoplastic resin powder having a primary particle size of more than 5 μm, it has a compressibility of only 0.15 Mg / m 3 as compared with B Ex. 49 containing the same lubricant. Low. Since the B ratio 21 is such that the average aggregation diameter of the thermoplastic resin powder exceeds 50 μm,
The tensile strength is 400 for all the mixtures of B-44-77.
440 MPa, whereas the mixture having a B ratio of 21 decreased to 370 MPa. Further, the mixture having a B ratio of 22 has a high extraction output when the total amount of the lubricant other than the thermoplastic resin powder added is less than 0.1% by weight, and the mixture having a B ratio of 23 has a total addition amount of the lubricant. Is more than 1% by weight, so that the fluidity and the hopper discharge property are poor.
【0061】[0061]
【発明の効果】以上述べたように、本発明により、金属
元素を含まない潤滑剤を使用し、焼結炉を汚染せず、ま
た従来の混合物と同等の抜出力やC付着度を維持して、
流動性やホッパ排出性に優れた粉末冶金用鉄基粉末混合
物及びその製造方法を提供できるようになった。As described above, according to the present invention, a lubricant containing no metal element is used, does not contaminate the sintering furnace, and maintains the same extraction force and C adhesion as the conventional mixture. hand,
It has become possible to provide an iron-based powder mixture for powder metallurgy excellent in fluidity and hopper discharge, and a method for producing the same.
【図1】熱可塑性樹脂粉末の凝集粒子を示す図である。FIG. 1 is a diagram showing aggregated particles of a thermoplastic resin powder.
1 一次粒子 2 凝集粒子 3 一次粒径 4 凝集粒径 1 primary particle 2 aggregated particle 3 primary particle size 4 aggregated particle size
フロントページの続き (72)発明者 尾崎 由紀子 千葉県千葉市中央区川崎町1番地 川崎製 鉄株式会社技術研究所内 (72)発明者 小倉 邦明 千葉県千葉市中央区川崎町1番地 川崎製 鉄株式会社技術研究所内 (72)発明者 永瀬 敏夫 神奈川県川崎市川崎区夜光1丁目2番1号 ゼオン化成株式会社川崎研究所内 (72)発明者 小林 健男 東京都港区芝公園2丁目4番1号 ゼオン 化成株式会社内 Fターム(参考) 4K018 AA24 AB05 AB07 AC01 BA13 BC01 BC12 BC15 BC30 CA09Continuing from the front page (72) Inventor Yukiko Ozaki 1 Kawasaki-cho, Chuo-ku, Chiba-shi, Chiba In the Technical Research Institute of Kawasaki Steel (72) Kuniaki Ogura 1 Kawasaki-cho, Chuo-ku, Chiba-shi, Chiba Kawasaki Steel (72) Inventor Toshio Nagase 1-2-1, Yoko, Kawasaki-ku, Kawasaki City, Kanagawa Prefecture Inside Kawasaki Research Laboratory, ZEON Kasei Co., Ltd. (72) Takeo Kobayashi, 2-4-1 Shiba Park, Minato-ku, Tokyo Zeon Kasei Co., Ltd. F term (reference) 4K018 AA24 AB05 AB07 AC01 BA13 BC01 BC12 BC15 BC30 CA09
Claims (10)
ビニル化合物の中から選ばれた少なくとも1種の単量体
単位を50重量%以上含有し、1次平均粒径が0.03
〜5μm、凝集平均粒径が5〜50μm、溶液比粘度法
で測定した平均分子量が3万〜500万の熱可塑性樹脂
粉末0.05重量%以上0.50重量%以下とを含むこ
とを特徴とする粉末冶金用鉄基粉末混合物。1. An iron-based powder comprising at least 50% by weight of at least one monomer unit selected from an acrylate ester, a methacrylate ester and an aromatic vinyl compound; 0.03
Thermoplastic resin powder having an average molecular weight of 30,000 to 5,000,000 measured by a solution specific viscosity method of 0.05 to 0.50% by weight. An iron-based powder mixture for powder metallurgy.
潤滑剤0.1重量%以上1.0重量%以下と、 前記潤滑剤により前記鉄基粉末に付着した合金用粉末及
び/又は切削性改善用粉末と、 アクリル酸エステル、メタクリル酸エステル及び芳香族
ビニル化合物の中から選ばれた少なくとも1種の単量体
単位を50重量%以上含有し、1次平均粒径が0.03
〜5μm、凝集平均粒径が5〜50μm、溶液比粘度法
で測定した平均分子量が3万〜500万の熱可塑性樹脂
粉末0.05重量%以上0.50重量%以下とを含むこ
とを特徴とする粉末冶金用鉄基粉末混合物。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。2. An iron-based powder; 0.1% by weight or more and 1.0% by weight or less of one or more lubricants selected from the following attached to the iron-based powder; Contains 50% by weight or more of alloy powder and / or powder for improving machinability attached to the base powder and at least one monomer unit selected from acrylates, methacrylates and aromatic vinyl compounds And the primary average particle size is 0.03
Thermoplastic resin powder having an average molecular weight of 30,000 to 5,000,000 measured by a solution specific viscosity method of 0.05 to 0.50% by weight. An iron-based powder mixture for powder metallurgy. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
ら選ばれた1種以上の潤滑剤の粉末0.5重量%以下を
含むことを特徴とする粉末冶金用鉄基粉末混合物。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。3. The iron-based powder mixture for powder metallurgy according to claim 2, further comprising 0.5% by weight or less of a powder of one or more lubricants selected from the following. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
イン酸、スピンドル油、タービン油の内から選ばれた1
種以上の有機質液体潤滑剤0.01重量%以上0.3重
量%以下を含むことを特徴とする粉末冶金用鉄基粉末混
合物。4. In addition to claim 2 or 3, further selected from oleic acid, spindle oil and turbine oil.
An iron-based powder mixture for powder metallurgy comprising at least 0.01% by weight and at most 0.3% by weight of at least one kind of organic liquid lubricant.
量%以上1.0重量%以下と、 アクリル酸エステル、メタクリル酸エステル及び芳香族
ビニル化合物の中から選ばれた少なくとも1種の単量体
単位を50重量%以上含有し、1次平均粒径が0.03
〜5μm、凝集平均粒径が5〜50μm、溶液比粘度法
で測定した平均分子量が3万〜500万の熱可塑性樹脂
粉末0.05重量%以上0.50重量%以下とを含むこ
とを特徴とする粉末冶金用鉄基粉末混合物。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。5. An iron-based powder, a powder for alloying and / or a powder for improving machinability, and a powder of at least one lubricant selected from the group consisting of 0.1% by weight or more and 1.0% by weight or less. And at least one monomer unit selected from acrylates, methacrylates and aromatic vinyl compounds in an amount of 50% by weight or more, and a primary average particle size of 0.03
Thermoplastic resin powder having an average molecular weight of 30,000 to 5,000,000 measured by a solution specific viscosity method of 0.05 to 0.50% by weight. An iron-based powder mixture for powder metallurgy. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
メチルであることを特徴とする請求項1〜5のいずれか
に記載の粉末冶金用鉄基粉末混合物。6. The iron-based powder mixture for powder metallurgy according to claim 1, wherein the thermoplastic resin powder is polymethyl methacrylate.
性改善用粉末と、下記の内から選ばれた1種以上の潤滑
剤0.1重量%以上1.0重量%以下とを混合した後、 その混合物を、さらに、前記潤滑剤が1種の場合は、該
潤滑剤の融点より10℃以上100℃以下高い温度で、
前記潤滑剤が2種以上からなる場合は、該潤滑剤の最低
の融点より10℃以上高く、最高の融点以下の温度で加
熱しながら混合し、 引き続き冷却して、前記鉄基粉末に前記合金用粉末及び
/又は切削性改善用粉末を溶融した前記潤滑剤により付
着した後、 この付着処理後の混合物に、アクリル酸エステル、メタ
クリル酸エステル及び芳香族ビニル化合物の中から選ば
れた少なくとも1種の単量体単位を50重量%以上含有
し、1次平均粒径が0.03〜5μm、凝集平均粒径が
5〜50μm、溶液比粘度法で測定した平均分子量が3
万〜500万の熱可塑性樹脂粉末0.05重量%以上
0.50重量%以下を混合することを特徴とする粉末冶
金用鉄基粉末混合物の製造方法。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。7. An iron-based powder, an alloy powder and / or a machinability improving powder, and 0.1% by weight or more and 1.0% by weight or less of one or more lubricants selected from the following: After mixing, the mixture is further heated at a temperature higher than the melting point of the lubricant by 10 ° C. or more and 100 ° C. or less when the lubricant is one kind,
When the lubricant is composed of two or more kinds, the mixture is heated and mixed at a temperature higher than the lowest melting point of the lubricant by 10 ° C. or higher and lower than the highest melting point. After the powder for use in grinding and / or the powder for improving machinability is adhered by the molten lubricant, the mixture after the adhering treatment is mixed with at least one selected from acrylates, methacrylates and aromatic vinyl compounds. Having a primary average particle size of 0.03 to 5 μm, an aggregation average particle size of 5 to 50 μm, and an average molecular weight of 3 measured by a solution specific viscosity method.
A method for producing an iron-based powder mixture for powder metallurgy, comprising mixing 0.05 to 0.50% by weight of thermoplastic resin powder of 10,000 to 5,000,000. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
性改善用粉末と、下記の内から選ばれた1種以上の潤滑
剤0.1重量%以上1.0重量%以下と、オレイン酸、
スピンドル油、タービン油の内から選ばれた1種以上の
有機質液体潤滑剤0.01重量%以上0.3重量%以下
とを混合した後、 その混合物を、さらに、前記潤滑剤が1種の場合は、該
潤滑剤の融点より10℃以上100℃以下高い温度で、
前記潤滑剤が2種以上からなる場合は、最低の融点の1
0℃以上最高の融点以下の温度で加熱しながら混合し、 引き続き冷却して、前記鉄基粉末に前記合金用粉末及び
/又は切削性改善用粉末を溶融した前記潤滑剤により付
着した後、 この付着処理後の混合物に、アクリル酸エステル、メタ
クリル酸エステル及び芳香族ビニル化合物の中から選ば
れた少なくとも1種の単量体単位を50重量%以上含有
し、1次平均粒径が0.03〜5μm、凝集平均粒径が
5〜50μm、溶液比粘度法で測定した平均分子量が3
万〜500万の熱可塑性樹脂粉末0.05重量%以上
0.50重量%以下を混合することを特徴とする粉末冶
金用鉄基粉末混合物の製造方法。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド。8. An iron-based powder, a powder for alloying and / or a powder for improving machinability, and 0.1% by weight or more and 1.0% by weight or less of one or more lubricants selected from the following: oleic acid,
After mixing at least 0.01% by weight or more and at most 0.3% by weight of an organic liquid lubricant selected from spindle oil and turbine oil, the mixture is further mixed with one type of lubricant. In this case, at a temperature higher than the melting point of the lubricant by 10 ° C or more and 100 ° C or less,
When the lubricant is composed of two or more kinds, the lowest melting point of 1
After mixing while heating at a temperature of 0 ° C. or higher and lower than the maximum melting point, followed by cooling, the powder for alloying and / or the powder for improving machinability is adhered to the iron-based powder by the molten lubricant. The mixture after the adhesion treatment contains at least one monomer unit selected from an acrylate ester, a methacrylate ester, and an aromatic vinyl compound in an amount of 50% by weight or more, and has a primary average particle size of 0.03% or more. -5 μm, agglomeration average particle size is 5-50 μm, average molecular weight measured by solution specific viscosity method is 3
A method for producing an iron-based powder mixture for powder metallurgy, comprising mixing 0.05 to 0.50% by weight of thermoplastic resin powder of 10,000 to 5,000,000. Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide.
の混合物に、さらに、下記の内から選ばれた1種以上の
潤滑剤の粉末0.5重量%以下を加えて、混合すること
を特徴とする粉末冶金用鉄基粉末混合物の製造方法。 記 ステアリン酸、オレイン酸アミド、ステアリン酸アミ
ド、ステアリン酸アミドとエチレンビスステアリン酸ア
ミドとの溶融混合物、エチレンビスステアリン酸アミ
ド、分子量1万以下のポリエチレン、エチレンビスステ
アリン酸アミドと分子量1万以下のポリエチレンとの溶
融混合物。9. The mixture after the adhesion treatment described in claim 7 or 8 is further mixed with 0.5% by weight or less of one or more lubricant powders selected from the following. A method for producing an iron-based powder mixture for powder metallurgy, comprising: Note stearic acid, oleic acid amide, stearic acid amide, a molten mixture of stearic acid amide and ethylenebisstearic acid amide, ethylenebisstearic acid amide, polyethylene with a molecular weight of 10,000 or less, ethylenebisstearic acid amide with a molecular weight of 10,000 or less Melt mixture with polyethylene.
酸メチルであることを特徴とする請求項7〜9のいずれ
かに記載の粉末冶金用鉄基粉末混合物の製造方法。10. The method for producing an iron-based powder mixture for powder metallurgy according to claim 7, wherein the thermoplastic resin powder is polymethyl methacrylate.
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JP9-295662 | 1997-10-28 | ||
JP10-198081 | 1998-06-30 | ||
JP19808198 | 1998-06-30 | ||
JP23841398A JP3887495B2 (en) | 1997-08-29 | 1998-08-25 | Iron-based powder mixture for powder metallurgy and method for producing the same |
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JP2010007176A (en) * | 2008-05-27 | 2010-01-14 | Jfe Steel Corp | Iron-based powdery mixture for powder metallurgy |
WO2011122230A1 (en) * | 2010-03-31 | 2011-10-06 | 出光興産株式会社 | Metallurgical lubricant powder and metal powder composition |
JP2013112824A (en) * | 2011-11-25 | 2013-06-10 | Jfe Steel Corp | Method for manufacturing iron-based powder for powder metallurgy and iron-based powder for powder metallurgy |
WO2014136554A1 (en) * | 2013-03-04 | 2014-09-12 | 株式会社神戸製鋼所 | Binder for powder metallurgy, mixed powder for powder metallurgy, and sintered body |
-
1998
- 1998-08-25 JP JP23841398A patent/JP3887495B2/en not_active Expired - Lifetime
Cited By (9)
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JP2010007176A (en) * | 2008-05-27 | 2010-01-14 | Jfe Steel Corp | Iron-based powdery mixture for powder metallurgy |
WO2011122230A1 (en) * | 2010-03-31 | 2011-10-06 | 出光興産株式会社 | Metallurgical lubricant powder and metal powder composition |
JP2011214033A (en) * | 2010-03-31 | 2011-10-27 | Idemitsu Kosan Co Ltd | Metallurgical lubricant and metal powder composition |
US9340743B2 (en) | 2010-03-31 | 2016-05-17 | Idemitsu Kosan Co., Ltd. | Metallurgical lubricant powder and metal powder composition |
JP2013112824A (en) * | 2011-11-25 | 2013-06-10 | Jfe Steel Corp | Method for manufacturing iron-based powder for powder metallurgy and iron-based powder for powder metallurgy |
WO2014136554A1 (en) * | 2013-03-04 | 2014-09-12 | 株式会社神戸製鋼所 | Binder for powder metallurgy, mixed powder for powder metallurgy, and sintered body |
JP2014196553A (en) * | 2013-03-04 | 2014-10-16 | 株式会社神戸製鋼所 | Binder for powder metallurgy, mixed powder for powder metallurgy and sintered body |
CN105008072A (en) * | 2013-03-04 | 2015-10-28 | 株式会社神户制钢所 | Binder for powder metallurgy, mixed powder for powder metallurgy, and sintered body |
US10240032B2 (en) | 2013-03-04 | 2019-03-26 | Kobe Steel, Ltd. | Binder for powder metallurgy, mixed powder for powder metallurgy, and sintered body |
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