KR20060136332A - Method of making a cemented carbide powder mixture - Google Patents
Method of making a cemented carbide powder mixture Download PDFInfo
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- KR20060136332A KR20060136332A KR1020060058129A KR20060058129A KR20060136332A KR 20060136332 A KR20060136332 A KR 20060136332A KR 1020060058129 A KR1020060058129 A KR 1020060058129A KR 20060058129 A KR20060058129 A KR 20060058129A KR 20060136332 A KR20060136332 A KR 20060136332A
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- cemented carbide
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- fatty acid
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- 239000000843 powder Substances 0.000 title claims abstract description 37
- 239000000203 mixture Substances 0.000 title claims abstract description 17
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 4
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 33
- 239000000194 fatty acid Substances 0.000 claims abstract description 33
- DPUOLQHDNGRHBS-KTKRTIGZSA-N Erucic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-KTKRTIGZSA-N 0.000 claims abstract description 32
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 19
- 239000011230 binding agent Substances 0.000 claims abstract description 17
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 17
- -1 fatty acid esters Chemical class 0.000 claims abstract description 16
- 238000003825 pressing Methods 0.000 claims abstract description 15
- 239000002253 acid Substances 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 8
- 239000011780 sodium chloride Substances 0.000 claims abstract description 8
- 125000002511 behenyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims abstract description 6
- 239000000956 alloy Substances 0.000 claims abstract description 4
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 4
- REDXJYDRNCIFBQ-UHFFFAOYSA-N aluminium(3+) Chemical class [Al+3] REDXJYDRNCIFBQ-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000002245 particle Substances 0.000 claims description 20
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 6
- 229910052803 cobalt Inorganic materials 0.000 claims description 6
- 239000010941 cobalt Substances 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 5
- 239000000654 additive Substances 0.000 claims description 4
- 239000003966 growth inhibitor Substances 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 4
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- ONCXFUAOAOCNRC-QZOPMXJLSA-N (Z)-docos-13-enoic acid;(Z)-octadec-9-enoic acid Chemical class CCCCCCCC\C=C/CCCCCCCC(O)=O.CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O ONCXFUAOAOCNRC-QZOPMXJLSA-N 0.000 claims description 2
- 150000004668 long chain fatty acids Chemical class 0.000 claims description 2
- 235000021281 monounsaturated fatty acids Nutrition 0.000 claims description 2
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 claims description 2
- 235000003441 saturated fatty acids Nutrition 0.000 claims description 2
- 150000004671 saturated fatty acids Chemical class 0.000 claims description 2
- 238000007906 compression Methods 0.000 abstract description 3
- 239000002002 slurry Substances 0.000 abstract description 3
- 238000001694 spray drying Methods 0.000 abstract description 3
- 239000002202 Polyethylene glycol Substances 0.000 description 16
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N Oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 4
- QIQXTHQIDYTFRH-UHFFFAOYSA-N Stearic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 4
- 239000011651 chromium Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- 238000000227 grinding Methods 0.000 description 4
- 238000005245 sintering Methods 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- UKMSUNONTOPOIO-UHFFFAOYSA-N Behenic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 description 2
- 239000005642 Oleic acid Substances 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- 238000005056 compaction Methods 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- 235000021357 Behenic acid Nutrition 0.000 description 1
- 206010022114 Injury Diseases 0.000 description 1
- UONOETXJSWQNOL-UHFFFAOYSA-N Tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 description 1
- 241000234314 Zingiber Species 0.000 description 1
- 235000006886 Zingiber officinale Nutrition 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 229940116226 behenic acid Drugs 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 229950008690 docosanoic acid Drugs 0.000 description 1
- 235000008397 ginger Nutrition 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000002105 nanoparticle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium(0) Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Abstract
본 발명은 초경 합금을 제조하는 방법에 관한 것으로, 경질 성분을 형성하는 분말 및 바인더상을 형성하는 분말을 가압제와 함께 습식 분쇄한다. 슬러리는 바람직하게는 분무 건조로 건조되며 소망하는 형상체로 압착되어 소결된다. 하기의 조성을 갖는 1 ~ 3 중량% 의 가압제를 사용하여, 18% 수축시 소정의 중량에서 압착압이 감소된 초경 합금 분말이 얻어질 수 있다.BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a cemented carbide, wherein the powder forming the hard component and the powder forming the binder phase are wet milled together with the pressure agent. The slurry is preferably dried by spray drying and pressed into a desired shape and sintered. Using 1 to 3% by weight of the pressurizing agent having the following composition, a cemented carbide powder with reduced compression pressure at a predetermined weight upon 18% shrinkage can be obtained.
- 90 중량% 이하의 PEG 및Up to 90% PEG by weight and
- C≥20 의 긴 사슬의 10 중량% 이상의 지방산, 지방산 에스테르 및 지방산 염, 특히 에루크산 및/또는 베헤닐산At least 10% by weight of fatty acids, fatty acid esters and fatty acid salts, in particular erucic acid and / or behenyl acid, of long chains of C ≧ 20;
본 발명은 또한 낮은 압착압으로 가압된 초경 합금 분말에 관한 것이다.The present invention also relates to cemented carbide alloy powder with low pressing pressure.
Description
본 발명은 낮은 압착압으로 초경합금 분말, 보다 자세하게는 초미립 및 나노 크기의 분말을 제조하는 방법에 관한 것이다.The present invention relates to a process for producing cemented carbide powder, more particularly ultrafine and nano-sized powder, at low pressing pressure.
경질 성분을 형성하는 분말, 바인더상을 형성하는 분말, 및 가압제 (일반적으로 PEG (폴리에틸렌 글리콜)) 를 습식 분쇄하여 슬러리를 만들고, 이 슬러리를 통상적으로 분무 건조로 건조시키며, 건조된 분말을 소망하는 형상체로 공구 가압하고, 마지막으로 소결함으로써 초경합금이 제조된다. 소결시, 상기 형상체는 약 16 ~ 20% 로 선형적으로 수축하게 된다. 이러한 수축은 생형체 (= "생밀도 (green density)") 를 형성하기 위해 분말의 압착시 얻어지는 이론 밀도(%) 에 따라 변하고, 또한 이론 밀도는 가압력, WC 입도, 입도의 분포, Co 함량, 및 가압제에 따라 변한다. 가압 공구는 그 제조가 값비싸고 따라서 18% 등의 표준 수축을 얻을 수 있도록 만들어진다. 이러한 수축은 소망하는 생밀도를 부여하도록 압착체에 충분한 가압력을 가함으로써 얻어진다. 연삭 등의 값비싼 소결 후속 작업을 피하기 위해 소결체의 크기를 가능한 소망하는 크기에 근접하도록 하는 것 이 매우 중요하다. 하지만, 입도가 미세하면, 예를 들어 마이크론 이하이면, 필요한 수축을 얻기 위해서는 더 큰 가압력이 필요하게 된다. 산업분야에서, 입도를 감소시킨 탄화물 분말내의 내부 마찰을 증가시키면 내압착성이 더 커지게 된다. 가압체내의 균열 또는 기공 등의 가압 결함의 위험성, 가압 공구의 비정상적 마모, 및 심지어 상해를 포함하는 가압 공구의 파괴 위험성이 높아지기 때문에 높은 가압력은 바람직하지 않다. 또한, 가압력을 소정의 소망하는 실행가능한 범위로 유지하면, 소결부의 치수 제어가 용이해진다.Powders that form hard components, powders that form a binder phase, and pressurizers (typically PEG (polyethylene glycol)) are wet pulverized to form a slurry, which is typically dried by spray drying, and the dried powder is desired. Carbide alloy is manufactured by tool pressurizing to a shape to make, and finally sintering. Upon sintering, the shaped body contracts linearly at about 16-20%. This shrinkage varies with the theoretical density (%) obtained upon compaction of the powder to form a green body (= "green density"), and the theoretical density also depends on the pressing force, WC particle size, distribution of particle size, Co content, And pressurizing agent. Pressing tools are made to be expensive to manufacture and thus obtain a standard shrinkage of 18% or the like. Such shrinkage is obtained by applying sufficient pressing force to the compact to give the desired biodensity. It is very important to keep the size of the sintered body as close to the desired size as possible to avoid costly subsequent sintering operations such as grinding. However, if the particle size is fine, for example, below micron, a larger pressing force is required to obtain the required shrinkage. In industry, increasing the internal friction in carbide powders with reduced particle sizes results in greater compression resistance. High pressing forces are undesirable because of the increased risk of press defects such as cracks or pores in the press body, abnormal wear of the press tool, and even damage to the press tool, including injury. In addition, if the pressing force is maintained in a predetermined desired range, the sintering portion can be easily controlled in size.
지방산, 지방산 염 및 지방산 에스테르는 산업분야에서 오랫동안 그 윤활성이 있는 것으로 알려져 있었다. 이들은 종종 그 탄소 사슬의 길이에 의해 특징지워진다. 올레산 및 스테아르산 둘다는 종종 C-18 이라고 하는 18 개의 탄소 사슬 등가물이며, 에루크산 및 베헤닐산은 자연적으로 생성되는 지방산 (C-22) 내의 가장 긴 탄소 사슬 중 하나를 가진다.Fatty acids, fatty acid salts and fatty acid esters have long been known for their lubricity in the industry. They are often characterized by the length of their carbon chains. Both oleic acid and stearic acid are 18 carbon chain equivalents, often referred to as C-18, and erucic acid and behenyl acid have one of the longest carbon chains in naturally occurring fatty acids (C-22).
초미립 초경 합금에 대한 압착압을 감소시키는 방법이 유럽특허공개 제 1043413 호에 개시되어 있다. 이 방법은, 약 3 시간 동안 WC 를 제외한 모든 성분을 예혼합하는 단계, WC 분말을 첨가하는 단계, 그 후 마지막으로 약 10 시간 동안 분쇄하는 단계로 이루어진다.A method for reducing the compaction pressure on ultrafine cemented carbide is disclosed in EP 1043413. The method consists of premixing all components except WC for about 3 hours, adding the WC powder and then finally grinding for about 10 hours.
본 발명의 목적은 미립의 초경 합금을 제조할 때 가압력을 감소시키는 방법을 제공하는 것이다.It is an object of the present invention to provide a method for reducing the pressing force when producing particulate cemented carbide.
본 발명의 방법에 따르면, 경질 성분을 형성하는 분말 및 바인더상을 형성하는 분말을 특정의 가압제와 함께 습식 분쇄한 후, 양호한 유동 특성을 가진 응집체 가 형성되도록 슬러리를 바람직하게는 분무 건조로 건조시킴으로써, 초경합금 분말이 제조된다.According to the method of the present invention, the powder forming the hard component and the powder forming the binder phase are wet pulverized with a specific pressurizing agent, and then the slurry is preferably dried by spray drying so that aggregates having good flow characteristics are formed. By doing so, cemented carbide powder is produced.
놀랍게도, 하기의 조성을 갖는 1 ~ 3 중량% 의 가압제를 사용함으로써 18% 수축으로 소정의 중량에서 압착압이 감소된 초경 합금 분말이 얻어질 수 있음을 알았다.Surprisingly, it was found that by using 1 to 3% by weight of the pressurizing agent having the following composition, a cemented carbide powder having a reduced compression pressure at a predetermined weight with 18% shrinkage can be obtained.
- 90 중량% 이하의 PEG 및Up to 90% PEG by weight and
- C≥20 의 긴 사슬의 10 중량% 이상의 지방산, 지방산 에스테르 및 지방산 염,At least 10% by weight of fatty acids, fatty acid esters and fatty acid salts of long chains of C ≧ 20,
- 바람직하게는 90 내지 60 중량%, 가장 바람직하게는 90 내지 65 중량% 의 PEG 및Preferably 90 to 60% by weight, most preferably 90 to 65% by weight of PEG and
- 바람직하게는 10 내지 40 중량%, 가장 바람직하게는 10 내지 35 중량% 의 지방산, 지방산 에스테르 및 지방산 염.Preferably from 10 to 40% by weight, most preferably from 10 to 35% by weight of fatty acids, fatty acid esters and fatty acid salts.
일 실시형태에 있어서, 포화 지방산, 고도 불포화 지방산, 특히 단일 불포화 지방산이 사용되고, 다른 실시형태에 있어서, 2 개의 산기를 갖는 긴 사슬 지방산이 사용된다.In one embodiment, saturated fatty acids, polyunsaturated fatty acids, in particular monounsaturated fatty acids are used and in other embodiments long chain fatty acids having two acid groups are used.
바람직한 실시형태에 있어서, 상기 지방산은 에루크산 (erucic acid) 및/또는 베헤닐산 (behenic acid) 이다.In a preferred embodiment, the fatty acid is erucic acid and / or behenic acid.
본 발명의 방법은 어떠한 초경 합금 조성물에도 적용될 수 있지만, 바람직하 게는 WC 및 통상적으로는 코발트인 바인더로서 니켈 또는 철 등의 첨가제와 합금화될 수 있는 2 ~ 20 중량% 의 바인더, 바람직하게는 입자 성장 억제제, 특히 1 중량% 미만의 Cr 및 1 중량% 미만의 V 를 가진 6 ~ 12 중량% 의 바인더를 포함하는 초경합금에 적용된다. 바람직하게는, WC 입자는 0.1 ~ 1.0 ㎛, 바람직하게는 0.2 ~ 0.6 ㎛ 의 평균 입도를 갖고, 실질적으로 1.5 ㎛ 를 초과하는 크기의 WC 입자를 갖지 않는다.Although the process of the present invention can be applied to any cemented carbide composition, it is preferably a binder of 2 to 20% by weight, preferably particles, which can be alloyed with additives such as nickel or iron as a binder which is WC and usually cobalt. It applies to growth inhibitors, in particular cemented carbides comprising from 6 to 12% by weight of binders having less than 1% by weight of Cr and less than 1% by weight of V. Preferably, the WC particles have an average particle size of 0.1 to 1.0 μm, preferably 0.2 to 0.6 μm, and have no WC particles of size substantially greater than 1.5 μm.
본 발명은 하기의 조성을 갖는 1 ~ 3 중량% 의 가압제를 포함하는 낮은 압착압으로 가압 준비된 초경 합금 분말에 관한 것이다.The present invention relates to a cemented carbide powder prepared by pressurization at a low pressing pressure comprising 1-3 wt% of a pressurizing agent having the following composition.
- 90 중량% 이하의 PEG 및Up to 90% PEG by weight and
- C≥20 의 긴 사슬의 10 중량% 이상의 지방산, 지방산 에스테르 및 지방산 염,At least 10% by weight of fatty acids, fatty acid esters and fatty acid salts of long chains of C ≧ 20,
- 바람직하게는 90 내지 60 중량%, 가장 바람직하게는 90 내지 65 중량% 의 PEC-Preferably 90 to 60% by weight, most preferably 90 to 65% by weight of PEC
- 바람직하게는 10 내지 40 중량%, 가장 바람직하게는 10 내지 35 중량% 의 지방산, 지방산 에스테르 및 지방산 염.Preferably from 10 to 40% by weight, most preferably from 10 to 35% by weight of fatty acids, fatty acid esters and fatty acid salts.
에루크산 및/또는 베헤닐산이 바람직한 지방산이다. 초경 합금 분말은, WC 및 통상적으로는 코발트인 바인더로서 니켈 또는 철 등의 첨가제와 합금화될 수 있는 2 ~ 20 중량% 의 바인더, 바람직하게는 입자 성장 억제제, 특히 1 중량% 미만의 Cr 및 1 중량% 미만의 V 를 가진 6 ~ 12 중량% 의 바인더를 포함하는 조성물을 구비한다. WC 입자는 0.1 ~ 1.0 ㎛, 바람직하게는 0.2 ~ 0.6 ㎛ 범위의 평균 입도를 가지는 것이 바람직하고, 실질적으로 1.5 ㎛ 를 초과하는 크기의 WC 입자를 갖지 않는다.Erucic acid and / or behenyl acid are preferred fatty acids. Cemented carbide powder is a binder of WC and usually cobalt, which can be alloyed with additives such as nickel or iron, from 2 to 20% by weight of binder, preferably particle growth inhibitors, in particular less than 1% by weight of Cr and 1% A composition comprising 6-12% by weight of a binder having a V of less than%. The WC particles preferably have an average particle size in the range of 0.1 to 1.0 μm, preferably 0.2 to 0.6 μm, and do not have WC particles of a size substantially greater than 1.5 μm.
실시예Example 1 One
10 중량% 코발트, 1 중량% 미만의 크롬 및 잔부로서 0.4 ㎛ 의 탄화텅스텐 (WC) 분말로 이루어진 조성을 가진 초미립 초경합금 혼합물이, PEG 및 에루크산의 다양한 혼합물을 사용하여 본 발명에 따라서 제조되며, 각 혼합물의 총량은 분말중량의 +2 중량% 이다. 에탄올 등에서 분쇄가 실시되었다.Ultrafine cemented carbide mixtures having a composition consisting of 10 wt% cobalt, less than 1 wt% chromium and 0.4 μm tungsten carbide (WC) powder as the balance are prepared according to the invention using various mixtures of PEG and erucic acid. , The total amount of each mixture is + 2% by weight of the powder weight. Grinding was carried out in ethanol and the like.
18% 의 소결 수축을 위한 가압력이 측정되었다.The pressing force for 18% sinter shrinkage was measured.
PEG(중량%) 에루크산(중량%) 18% 수축 압력(MPa)PEG (% by weight) Erucic acid (% by weight) 18% Shrinkage pressure (MPa)
2.0 0 135 (종래기술)2.0 0 135 (Prior Art)
1.9 0.1 118 (본 발명 범위외)1.9 0.1 118 (outside the scope of the invention)
1.8 0.2 98 (본 발명)1.8 0.2 98 (invention)
1.6 0.4 78 (본 발명)1.6 0.4 78 (invention)
1.5 0.5 79 (본 발명)1.5 0.5 79 (invention)
WC 의 상기 입도에 대해서, 0.4 중량% PEG 와 에루크산과의 최적 교환으로 가압력을 42% 감소시켜 18% 소결 수축을 달성하였다.For this particle size of the WC, 18% sintered shrinkage was achieved by reducing the pressing force by 42% with an optimum exchange of 0.4% by weight PEG with erucic acid.
실시예Example 2 2
실시예 1 과 동일한 조성을 갖지만 입도가 0.2 ㎛ 인 더 미세한 WC 를 사용하여 초미립 초경합경 분말 혼합물이 본 발명에 따라 제조되었다. 본 실시예에서도, 에탄올에서 분쇄가 실시되었다. 각각 총량이 분말 중량의 +1.5 내지 +2 중량% 인 PEG 및 다른 지방산의 다양한 혼합물을 시험하였다. 4000 kg 의 일정한 최대 가압 하중은 매우 미세한 카바이드 분말내의 PS21 시험편을 19% 목표 수축 (즉, >190MPa) 으로 가압하기에 불충분하였다. 따라서, 가압 높이 및 수축은 경우당 2 개의 샘플 (소형의 스프레드를 갖춤) 에 대해 측정되었다.Ultrafine cemented carbide powder mixtures were prepared according to the present invention using finer WCs having the same composition as Example 1 but with a particle size of 0.2 μm. Also in this example, grinding was performed in ethanol. Various mixtures of PEG and other fatty acids were tested, each having a total amount of +1.5 to + 2% by weight of the powder weight. A constant maximum press load of 4000 kg was insufficient to pressurize the PS21 test piece in very fine carbide powder to 19% target shrinkage (ie,> 190 MPa). Thus, pressurization height and shrinkage were measured for two samples per case (with a small spread).
다음의 가압제를 사용하였다.The following pressurants were used.
PEG(중량%) 지방산(중량%) 가압 높이(mm) 수축(%)PEG (% by weight) Fatty acid (% by weight) Pressurized height (mm) Shrinkage (%)
2.0 - 7.34 23.42.0-7.34 23.4
1.5 0.5 올레산 7.22 23.01.5 0.5 Oleic Acid 7.22 23.0
1.5 0.5 스테아르산 7.22 23.11.5 0.5 Stearic Acid 7.22 23.1
1.5 0.5 에루크산 7.15 22.81.5 0.5 erucic acid 7.15 22.8
1.5 0.5 베헤닐산 7.15 22.81.5 0.5 Behenyl Acid 7.15 22.8
1.5 - 7.29 23.31.5-7.29 23.3
1.0 0.5 에루크산 6.92 21.91.0 0.5 Erucic acid 6.92 21.9
1.0 0.7 에루크산 6.81 21.41.0 0.7 erucic acid 6.81 21.4
0.5 1.0 에루크산 6.67 20.90.5 1.0 erucic acid 6.67 20.9
- 1.5 에루크산 6.59 20.71.5 erucic acid 6.59 20.7
더 긴 사슬 (C20 이상) 의 지방산이, 0.2 ㎛ 카바이드 분말을 가압하기 위한 윤활제로서 가장 효과적이고, PEG 없이 그 자체만으로 가장 효과적으로 사용됨을 알았다. 하지만, PEG 는 압착체에 더 나은 생강도 (green strength) 를 제공해주고, 그로 인해 PEG 일부를 보유할 필요가 있을 수 있다.It has been found that longer chain (more than C20) fatty acids are most effective as lubricants for pressurizing 0.2 μm carbide powders and are most effectively used on their own without PEG. However, PEG gives the green body better ginger strength, and therefore it may be necessary to retain some PEG.
실시예Example 3 3
7.0 중량% 코발트, 1.0 중량% 미만의 크롬, 1.0 중량% 바나듐 및 잔부로서 0.3 ㎛ 의 WC 분말로 이루어진 조성을 가진 초경합금 분말 혼합물이, 본 발명에 따라서 제조되었다. 1.5 중량% PEG 또는 1.0 중량% PEG + 0.5 중량% 에루크산이 혼합된 2 개의 경우를 시험하였다.A cemented carbide powder mixture having a composition consisting of 7.0 wt% cobalt, less than 1.0 wt% chromium, 1.0 wt% vanadium and WC powder of 0.3 μm as the balance was prepared according to the present invention. Two cases with 1.5 wt% PEG or 1.0 wt% PEG + 0.5 wt% erucic acid were tested.
PEG(중량%) 에루크산(중량%) 가압력(MPa) 수축(%)PEG (% by weight) Erucic acid (% by weight) Pressure (MPa) Shrinkage (%)
1.5 - >190 20.71.5-> 190 20.7
1.0 0.5 93 20.1(본발명)1.0 0.5 93 20.1 (invention)
본 발명에 의하면, 가압력을 감소시켜 미립의 초경 합금을 제조할 수 있다.According to the present invention, it is possible to produce fine cemented carbide by reducing the pressing force.
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US20090311124A1 (en) * | 2008-06-13 | 2009-12-17 | Baker Hughes Incorporated | Methods for sintering bodies of earth-boring tools and structures formed during the same |
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US4070184A (en) * | 1976-09-24 | 1978-01-24 | Gte Sylvania Incorporated | Process for producing refractory carbide grade powder |
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