TW201634682A - Heat treatment oil composition - Google Patents
Heat treatment oil composition Download PDFInfo
- Publication number
- TW201634682A TW201634682A TW105103121A TW105103121A TW201634682A TW 201634682 A TW201634682 A TW 201634682A TW 105103121 A TW105103121 A TW 105103121A TW 105103121 A TW105103121 A TW 105103121A TW 201634682 A TW201634682 A TW 201634682A
- Authority
- TW
- Taiwan
- Prior art keywords
- petroleum resin
- seconds
- oil composition
- heat treatment
- oil
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M159/00—Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M101/00—Lubricating compositions characterised by the base-material being a mineral or fatty oil
- C10M101/02—Petroleum fractions
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M143/00—Lubricating compositions characterised by the additive being a macromolecular hydrocarbon or such hydrocarbon modified by oxidation
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M159/00—Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
- C10M159/005—Macromolecular compounds, e.g. macromolecular compounds composed of alternatively specified monomers not covered by the same main group
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M159/00—Lubricating compositions characterised by the additive being of unknown or incompletely defined constitution
- C10M159/02—Natural products
- C10M159/04—Petroleum fractions, e.g. tars, solvents
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/56—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering characterised by the quenching agents
- C21D1/58—Oils
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/10—Petroleum or coal fractions, e.g. tars, solvents, bitumen
- C10M2203/1006—Petroleum or coal fractions, e.g. tars, solvents, bitumen used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/10—Petroleum or coal fractions, e.g. tars, solvents, bitumen
- C10M2203/102—Aliphatic fractions
- C10M2203/1025—Aliphatic fractions used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/003—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions used as base material
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2205/00—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
- C10M2205/02—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
- C10M2205/028—Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/02—Viscosity; Viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2020/00—Specified physical or chemical properties or characteristics, i.e. function, of component of lubricating compositions
- C10N2020/01—Physico-chemical properties
- C10N2020/04—Molecular weight; Molecular weight distribution
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2030/00—Specified physical or chemical properties which is improved by the additive characterising the lubricating composition, e.g. multifunctional additives
- C10N2030/02—Pour-point; Viscosity index
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/20—Metal working
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/20—Metal working
- C10N2040/24—Metal working without essential removal of material, e.g. forming, gorging, drawing, pressing, stamping, rolling or extruding; Punching metal
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/20—Metal working
- C10N2040/242—Hot working
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
- C10N2060/02—Reduction, e.g. hydrogenation
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Lubricants (AREA)
Abstract
Description
本發明是有關於熱處理油組成物。 This invention relates to heat treated oil compositions.
在鋼材等金屬材料方面,以改善其性質為目的會施以淬火、回火、退火、正常化等之熱處理。該等熱處理中,淬火是將業經加熱之金屬材料浸漬於冷卻劑中使之變態為預定之淬火組織的處理,利用該淬火,處理物會變得非常堅硬。例如,若是將呈沃斯田鐵狀態之經加熱鋼材浸漬於冷卻劑中,在上臨界冷卻速度以上進行冷卻,便可使之變態為麻田散鐵等淬火組織。 In the case of metal materials such as steel, heat treatment such as quenching, tempering, annealing, and normalization is applied for the purpose of improving the properties thereof. In these heat treatments, quenching is a treatment in which a heated metal material is immersed in a coolant to be transformed into a predetermined quenched structure, and the treated material becomes very hard by the quenching. For example, if the heated steel material in the Wolsfield state is immersed in the coolant and cooled above the upper critical cooling rate, it can be transformed into a quenched structure such as 麻田散铁.
冷卻劑一般可使用油系、水系之熱處理劑。若就使用油系之熱處理劑(熱處理油)的金屬材料淬火加以說明,以經加熱之金屬材料投入屬於冷卻劑之熱處理油的情況而言,通常是經過3個階段而予以冷卻。具體而言是(1)金屬材料被熱處理油蒸氣膜所包覆之第1階段(蒸氣膜階段)、(2)蒸氣膜破裂而發生沸騰之第2階段(沸騰階段)、(3)金屬材料溫度變為熱處理油沸點以下,而熱被對流帶走之第3階段(對流階段)。然後,各階段中由於金屬材料周圍的 環境氣體不同的緣故,冷卻速度各異,以第2階段(沸騰階段)之冷卻速度最大。 As the coolant, an oil-based or water-based heat treatment agent can be generally used. In the case of quenching a metal material using an oil-based heat treatment agent (heat treatment oil), in the case where a heat-treated oil belonging to a coolant is supplied to a heated metal material, it is usually cooled in three stages. Specifically, (1) the first stage (vapor film stage) in which the metal material is coated with the heat-treated oil vapor film, (2) the second stage in which the vapor film is broken to cause boiling (boiling stage), and (3) the metal material. The temperature becomes below the boiling point of the heat treatment oil, and the heat is taken away by the convection in the third stage (convection stage). Then, in each stage due to the surrounding metal material The cooling rate varies depending on the ambient gas, and the cooling rate in the second stage (boiling stage) is the largest.
一般而言,熱處理油中,從蒸氣膜階段移行至沸騰階段時冷卻速度會急遽加速。若金屬材料並非單純的平面形狀的情況,蒸氣膜階段與沸騰階段容易在金屬材料表面處於交混。然後,在該交混發生的情況下,因蒸氣膜階段與沸騰階段之冷卻速度差,金屬材料表面會產生極大的溫度差。然後,由於該溫度差,熱應力或變態應力油然而生,以致金屬材料產生應變。 In general, in the heat-treated oil, the cooling rate is rapidly accelerated from the vapor film stage to the boiling stage. If the metal material is not a simple planar shape, the vapor film stage and the boiling stage are likely to be intermixed on the surface of the metal material. Then, in the case where the mixing occurs, a large temperature difference occurs on the surface of the metal material due to the difference in the cooling rate between the vapor film stage and the boiling stage. Then, due to the temperature difference, thermal stress or abnormal stress is generated, so that the metal material is strained.
因此,在金屬材料之熱處理上,尤其是淬火方面,選定適於該熱處理條件之熱處理油就十分重要,若該選定不適當,則會有金屬材料產生應變且同時無法獲得充分淬火硬度之情形。 Therefore, in the heat treatment of the metal material, especially in the quenching, it is important to select the heat treatment oil suitable for the heat treatment condition. If the selection is not appropriate, there is a case where the metal material is strained and at the same time, sufficient hardening hardness cannot be obtained.
一方面,熱處理油依日本JIS K2242:2012被分類為1種至3種,使用於淬火者是1種之1號油、1種之2號油、2種之1號油、2種之2號油。其中在日本JIS K2242:2012已規範了從800℃起至400℃為止之冷卻秒以作為冷卻性能之指標,1種2號被定在4.0秒以下,2種1號被定在5.0秒以下,2種2號被定在6.0秒以下。該冷卻秒數愈短則冷卻性能愈高,金屬材料變得愈硬。 On the one hand, the heat-treated oil is classified into one to three kinds according to Japanese JIS K2242:2012, and the one used for quenching is one type 1 oil, one type of No. 2 oil, two kinds of No. 1 oil, and two kinds of two. No. oil. In Japan, JIS K2242:2012 has standardized the cooling seconds from 800 °C to 400 °C as an indicator of cooling performance. One type 2 is set to be 4.0 seconds or less, and two types of 1 number are set to 5.0 seconds or less. Two types of No. 2 are set to be below 6.0 seconds. The shorter the number of cooling seconds, the higher the cooling performance and the harder the metal material becomes.
一般而言,淬火後金屬之硬度與應變係呈制衡的關係,愈硬則應變愈大。 In general, the hardness of the metal after quenching is in balance with the strain system. The harder the strain, the greater the strain.
又,在工業性方面,也使用300℃秒數來作為顯示油劑冷卻性的指標。所謂300℃秒數,是依循日本JIS K2242:2012之冷卻性能測試方法而求得之冷卻曲線中從800℃起至300℃為止之冷卻時間。 Further, in terms of industrial properties, the number of seconds at 300 ° C was also used as an index indicating the cooling property of the oil agent. The so-called 300 ° C seconds is in accordance with Japanese JIS The cooling time from 800 ° C to 300 ° C in the cooling curve obtained by the cooling performance test method of K2242: 2012.
使用者為了獲得目的之硬度與應變,會以上述指標為基準選擇淬火油。例如,在應變會構成問題之汽車用齒輪零件等之淬火上,上述2種1號油廣為使用。這是由於以上述1種油而言應變會變大,再加上視零件會有硬度變得過高的緣故,又,以上述2種2號油而言雖然應變可變小,但硬度不足的緣故。 In order to obtain the hardness and strain of the purpose, the user selects the quenching oil based on the above indexes. For example, in the quenching of automobile gear parts and the like which have a problem in strain, the above-mentioned two types of No. 1 oil are widely used. This is because the strain is increased by the above-mentioned one type of oil, and the hardness of the parts is too high, and the strain is small, but the hardness is insufficient. The reason.
不過,汽車用變速器或減速器等的零件,幾乎都是大量生產,並進行在1個托架上層疊大量處理物一次進行淬火之所謂群淬火(group hardening)。這種情況下,視安置已層疊之零件的位置,會有冷卻性能產生不均、各個零件硬度或應變產生不均的問題。例如,安置於下部之零件硬度偏高,而安置於上部之零件硬度偏低等等情況。 However, parts such as an automobile transmission or a speed reducer are almost mass-produced, and so-called group hardening in which a large amount of processing material is stacked on one carrier and quenched once is performed. In this case, depending on the position where the stacked parts are placed, there is a problem that the cooling performance is uneven, and the hardness or strain of each part is uneven. For example, the hardness of the parts placed in the lower part is high, and the hardness of the parts placed in the upper part is low.
有鑑於以上狀況,遂有專利文獻1~6之技術的提案。 In view of the above situation, there are proposals for the techniques of Patent Documents 1 to 6.
專利文獻1:日本特開2003-286517號公報 Patent Document 1: Japanese Patent Laid-Open Publication No. 2003-286517
專利文獻2:日本特開2002-38214號公報 Patent Document 2: Japanese Laid-Open Patent Publication No. 2002-38214
專利文獻3:日本特開2001-152243號公報 Patent Document 3: Japanese Laid-Open Patent Publication No. 2001-152243
專利文獻4:日本特開2002-327191號公報 Patent Document 4: Japanese Laid-Open Patent Publication No. 2002-327191
專利文獻5:日本特開2007-9238號公報 Patent Document 5: Japanese Laid-Open Patent Publication No. 2007-9238
專利文獻6:日本特開2013-194262號公報 Patent Document 6: Japanese Laid-Open Patent Publication No. 2013-194262
為了降低群淬火時各個零件硬度或應變之不均,專利文獻1提案了追加振動機或噴射裝置等特殊設備。 In order to reduce unevenness in hardness or strain of each part during quenching, Patent Document 1 proposes to add special equipment such as a vibrating machine or an injection device.
然而,要在習知裝置追加上述設備會花費成本,而且視設備還會改造困難。因此,冀望有一種技術,不須如專利文獻1進行設備投資,而僅利用熱處理油組成物特性來減低硬度或應變的不均。 However, it is costly to add the above-mentioned equipment to the conventional device, and it is difficult to retrofit the device. Therefore, there is a need to have a technique that does not require investment in equipment as in Patent Document 1, but uses only heat treatment oil composition characteristics to reduce unevenness in hardness or strain.
此外,蒸氣膜階段一旦拉長,則蒸氣膜階段與沸騰階段交混的時間也跟著拉長,應變容易變大。因此,宜縮短到達蒸氣膜階段結束之溫度(特性溫度)為止的秒數(特性秒數)。 Further, once the vapor film stage is elongated, the time during which the vapor film stage and the boiling stage are mixed is also elongated, and the strain is liable to become large. Therefore, it is desirable to shorten the number of seconds (characteristic seconds) until the temperature (characteristic temperature) at which the vapor film stage ends.
為了消除特性秒數的影響,專利文獻2中提案一種利用氣體冷卻至特性溫度以下再接著進行油淬火之方法。 In order to eliminate the influence of the number of characteristic seconds, Patent Document 2 proposes a method of cooling with a gas to a temperature lower than a characteristic temperature and then performing oil quenching.
另一方面,為了消除冷卻不均造成的處理物溫度差,專利文獻3中提案一種在一達到麻田散鐵變態初始溫度以上即先暫自淬火油將處理物拉起以行均熱之方法。 On the other hand, in order to eliminate the difference in the temperature of the treated material caused by the uneven cooling, Patent Document 3 proposes a method of uniformly raising the treated material from the quenching oil at a temperature above the initial temperature of the metamorphic iron of the granulated iron.
然而,專利文獻2及3之手法,均較單純的油淬火更增成本或時間。又,專利文獻2及3之手法,是縮小應變的方法,並無法減少群淬火時各個零件硬度或應變之不均。 However, the methods of Patent Documents 2 and 3 are more costly or time-consuming than simple oil quenching. Further, the methods of Patent Documents 2 and 3 are methods for reducing strain, and it is not possible to reduce unevenness in hardness or strain of each part during group quenching.
專利文獻4中提案了一種熱處理油組成物,可用作在金屬材料淬火上使冷卻不均不易產生、可確保淬火處理物之硬度同時可減低淬火應變之熱處理油組成物,該熱處理油組成物是由混合基油構成,該混合基油係由在40℃下之動態黏度為5~60mm2/s之低黏度基油50~95重量%、及 在40℃下之動態黏度為300mm2/s以上之高黏度基油50~5重量%所構成。 Patent Document 4 proposes a heat-treating oil composition which can be used as a heat-treating oil composition which can prevent the unevenness of cooling from being generated on the quenching of a metal material, can ensure the hardness of the quenched material and can reduce the quenching strain, and the heat-treating oil composition It is composed of a mixed base oil which is 50~95% by weight of a low viscosity base oil having a dynamic viscosity of 5 to 60 mm 2 /s at 40 ° C and a dynamic viscosity of 300 mm 2 at 40 ° C / More than s high viscosity base oil 50~5 wt%.
又,專利文獻5中提案了一種熱處理油組成物,其具有與上述2種1號油相同程度的冷卻性能,卻又能減少群淬火時冷卻性能不均。具體而言,該熱處理油組成物含有混合基油,該混合基油係由5%餾出溫度在300℃以上且400℃以下之低沸點基油計5質量%以上且低於50質量%、及5%餾出溫度在500℃以上之高沸點基油計超過50質量%且在95%以下所構成。 Further, Patent Document 5 proposes a heat-treating oil composition which has the same cooling performance as the above-mentioned two types of No. 1 oil, but which can reduce the unevenness in cooling performance during group quenching. Specifically, the heat-treated oil composition contains a mixed base oil which is 5% by mass or more and less than 50% by mass based on a low-boiling base oil having a 5% distillation temperature of 300 ° C or more and 400 ° C or less. And a high-boiling base oil having a 5% distillation temperature of 500 ° C or more is more than 50% by mass and is composed of 95% or less.
然而,專利文獻4及5之熱處理油組成物並未使用蒸氣膜破裂劑,因此特性秒數長,無法減少群淬火時各個零件硬度或應變之不均。 However, since the heat treatment oil compositions of Patent Documents 4 and 5 do not use a vapor film breaker, the number of characteristics is long, and the unevenness of hardness or strain of each part during group quenching cannot be reduced.
專利文獻6中提案一種熱處理油組成物,其係摻混了以組成物總量基準計在50質量%以上且95質量%以下之40℃動態黏度為5mm2/s以上且60mm2/s以下之基油、以組成物總量基準計在5質量%以上且50質量%以下之40℃動態黏度為300mm2/s以上之基油、及α烯烴共聚物,藉此,可減少群淬火時冷卻性能不均。 Patent Document 6 proposes a heat-treating oil composition in which a dynamic viscosity at 40 ° C of 50% by mass or more and 95% by mass or less based on the total amount of the composition is 5 mm 2 /s or more and 60 mm 2 /s or less. when the base oil to the composition in a total amount of 5 mass% or more and 50 mass% or less of dynamic viscosity of less than 40 ℃ of 300mm 2 / s base oil, and α-olefin copolymer, whereby the quenching group may be reduced Uneven cooling performance.
然而,專利文獻6之熱處理油組成物,有著因進行反覆淬火以致冷卻性能經時性降低的問題。 However, the heat-treated oil composition of Patent Document 6 has a problem that the cooling performance is deteriorated with time by repeated quenching.
本發明便是在此狀況下完成者,本發明目的在於提供一種熱處理油組成物,在利用淬火等將金屬材料進行熱處理之際,可保有與JIS K2242:2012之2種1號油相同程度的冷卻性能,又可減少群淬火時各個零件冷卻性能不 均,同時可抑制在反覆進行該熱處理時發生的冷卻性能經時性變化。 The present invention has been made in view of the above, and it is an object of the present invention to provide a heat-treating oil composition which can maintain the same degree as the two types of No. 1 oil of JIS K2242:2012 when heat-treating a metal material by quenching or the like. Cooling performance can reduce the cooling performance of each part during group quenching At the same time, it is possible to suppress the temporal change of the cooling performance which occurs when the heat treatment is repeatedly performed.
為了解決上述課題,本發明之實施形態中,提供一種熱處理油組成物,其特徵在於含有:(A)基油;(B)選自於石油樹脂及/或石油樹脂衍生物之一種以上。該熱處理油組成物由冷卻曲線獲得之特性秒數在1.00秒以下,並且,該冷卻曲線從800℃起至300℃為止之冷卻時間即300℃秒數在6.00秒以上且14.50秒以下,其中該冷卻曲線係依循日本JIS K2242:2012之冷卻性能測試方法而求得。 In order to solve the above problems, an embodiment of the present invention provides a heat treatment oil composition comprising: (A) a base oil; and (B) one or more selected from the group consisting of petroleum resins and/or petroleum resin derivatives. The characteristic temperature of the heat-treated oil composition obtained from the cooling curve is 1.00 second or less, and the cooling time of the cooling curve from 800 ° C to 300 ° C, that is, 300 ° C seconds is 6.00 seconds or more and 14.50 seconds or less, wherein The cooling curve was obtained in accordance with the cooling performance test method of JIS K2242:2012, Japan.
本發明之熱處理油組成物,在利用淬火等將金屬材料進行熱處理之際,可保有與JIS K2242:2012之2種1號油相同程度的冷卻性能,又可減少群淬火時各個零件冷卻性能不均。進而,本發明之熱處理油組成物,可抑制在反覆進行金屬材料之熱處理時發生的冷卻性能經時性變化。 When the metal material is heat-treated by quenching or the like, the heat-treating oil composition of the present invention can maintain the same cooling performance as the two types of No. 1 oil of JIS K2242:2012, and can reduce the cooling performance of each part during group quenching. All. Further, the heat-treated oil composition of the present invention can suppress the change in the cooling performance which occurs when the metal material is repeatedly subjected to the heat treatment.
以下,說明本發明之實施形態。本實施形態之熱處理油組成物含有:(A)基油、(B)選自於石油樹脂及/或石油樹脂衍生物之一種以上,且由冷卻曲線獲得之特性秒數在1.00秒以下,並且,該冷卻曲線從800℃起至300℃為止之冷卻時間即300℃秒數在6.00秒以上且14.50秒以下,其中 該冷卻曲線係依循日本JIS K2242:2012之冷卻性能測試方法而求得。 Hereinafter, embodiments of the present invention will be described. The heat-treated oil composition of the present embodiment contains: (A) a base oil, (B) one or more selected from the group consisting of petroleum resins and/or petroleum resin derivatives, and the characteristic number of seconds obtained from the cooling curve is 1.00 second or less, and The cooling time of the cooling curve from 800 ° C to 300 ° C, that is, 300 ° C seconds is less than 6.00 seconds and less than 14.50 seconds, wherein This cooling curve was obtained in accordance with the cooling performance test method of JIS K2242:2012, Japan.
[(A)基油] [(A) base oil]
(A)成分之基油可舉礦油及/或合成油。 The base oil of the component (A) may be mineral oil and/or synthetic oil.
礦油可列舉:利用溶劑精煉、氫化精煉等一般精煉法製得之石蠟烴基系礦油、中間基系礦油及環烷基系礦油等;將已藉由費托氏法等製造之蠟(Gas-to-liquid wax)、礦油系蠟等之蠟進行異構化所製造之蠟異構化系油;等。 Examples of the mineral oil include a paraffinic hydrocarbon-based mineral oil, an intermediate-based mineral oil, and a naphthenic-based mineral oil obtained by a general refining method such as solvent refining and hydrogen refining; and a wax which has been produced by a Fischer-Tropsch method or the like ( Gas-to-liquid wax), a wax isomerization system oil produced by isomerization of a wax such as mineral oil wax, and the like.
合成油方面可列舉:烴系合成油、醚系合成油等。烴系合成油可列舉烷基苯、烷基萘等。醚系合成油可列舉聚氧伸烷二醇、聚苯醚等。 Examples of the synthetic oil include a hydrocarbon-based synthetic oil and an ether-based synthetic oil. The hydrocarbon-based synthetic oil may, for example, be an alkylbenzene or an alkylnaphthalene. Examples of the ether-based synthetic oil include polyoxyalkylene glycol and polyphenylene ether.
(A)成分之基油可以是僅使用上述礦油及合成油當中一種的單一系,也可以是如已將礦油之二種以上予以混合者、已將合成油之二種以上混合者、將礦油及合成油各一種或二種以上予以混合者般,為混合系。 The base oil of the component (A) may be a single system using only one of the above-mentioned mineral oils and synthetic oils, or may be a mixture of two or more kinds of mineral oils, or a mixture of two or more types of synthetic oils. A mixed system is used in which one type or two or more types of mineral oil and synthetic oil are mixed.
(A)成分之基油之40℃動態黏度以40mm2/s以上且500mm2/s以下為佳,50mm2/s以上且350mm2/s以下較佳,60mm2/s以上且200mm2/s以下更佳。 The 40 ° C dynamic viscosity of the base oil of the component (A) is preferably 40 mm 2 /s or more and 500 mm 2 /s or less, more preferably 50 mm 2 /s or more and 350 mm 2 /s or less, and 60 mm 2 /s or more and 200 mm 2 / s is better below.
藉由使(A)成分之基油之40℃動態黏度在上述範圍,可確保基於(A)所達到的本質性冷卻性能,而易於使特性秒數及300℃秒數在後述範圍。 By setting the 40 ° C dynamic viscosity of the base oil of the component (A) to the above range, the essential cooling performance achieved by (A) can be ensured, and the characteristic number of seconds and the number of 300 ° C seconds can be easily made in the range described later.
若(A)成分之基油為二種以上基油混合而得之基油,則混合基油之動態黏度以滿足上述範圍為佳。 When the base oil of the component (A) is a base oil obtained by mixing two or more base oils, the dynamic viscosity of the mixed base oil satisfies the above range.
又,本實施形態中,基油及熱處理油組成物之動態黏 度可依循JIS K2283:2000來測定。 Moreover, in the present embodiment, the dynamic viscosity of the base oil and the heat-treated oil composition The degree can be measured in accordance with JIS K2283:2000.
相對於熱處理油組成物總量計,(A)成分之基油之含有比率以10~99.9質量%為佳,50~98質量%較佳,80~95質量%更佳。 The content ratio of the base oil of the component (A) is preferably from 10 to 99.9% by mass, more preferably from 50 to 98% by mass, even more preferably from 80 to 95% by mass, based on the total amount of the heat-treated oil composition.
藉由使(A)成分之含有比率在80質量%以上,可確保基於(A)所達到的本質性冷卻性能,藉由使(A)成分之含有比率少於100質量%,可確保(B)成分之石油樹脂及/或石油樹脂衍生物的使用量,而易於獲得後述之基於(B)成分所達到的效果。 By setting the content ratio of the component (A) to 80% by mass or more, the essential cooling performance achieved by (A) can be ensured, and the content ratio of the component (A) can be ensured by less than 100% by mass. The amount of the petroleum resin and/or petroleum resin derivative used as the component is easy to obtain the effect achieved by the component (B) described later.
[(B)石油樹脂及/或石油樹脂衍生物] [(B) petroleum resin and / or petroleum resin derivatives]
本實施形態之熱處理油組成物含有一種以上之(B)石油樹脂及/或石油樹脂衍生物。(B)成分之石油樹脂及/或石油樹脂衍生物具有可作為蒸氣膜破裂劑之功能。 The heat-treated oil composition of the present embodiment contains one or more (B) petroleum resins and/or petroleum resin derivatives. The petroleum resin and/or petroleum resin derivative of the component (B) has a function as a vapor film breaker.
藉由使用石油樹脂及/或石油樹脂衍生物來作為蒸氣膜破裂劑,可縮短蒸氣膜階段,而易於使熱處理油組成物之冷卻性能與JIS K2242:2012之2種1號油相同程度。 By using a petroleum resin and/or a petroleum resin derivative as a vapor film breaker, the vapor film stage can be shortened, and the cooling performance of the heat treatment oil composition can be easily made to the same level as the two types of No. 1 oil of JIS K2242:2012.
又,由於藉由使用石油樹脂及/或石油樹脂衍生物可縮短蒸氣膜階段,因此蒸氣膜階段與沸騰階段不易在金屬材料表面交混。緣此,藉由使用石油樹脂及/或石油樹脂衍生物,不易發生群淬火時各個零件冷卻性能不均(硬度或應變之不均)。又,藉由使用石油樹脂及/或石油樹脂衍生物,在零件為複雜形狀的情況下,該零件各處之冷卻性能也不易發生不均,因此可抑制各零件之應變。 Further, since the vapor film stage can be shortened by using a petroleum resin and/or a petroleum resin derivative, the vapor film stage and the boiling stage are less likely to be mixed on the surface of the metal material. Therefore, by using a petroleum resin and/or a petroleum resin derivative, uneven cooling performance (uneven hardness or strain) of each part during group quenching is less likely to occur. Further, by using a petroleum resin and/or a petroleum resin derivative, when the parts have a complicated shape, the cooling performance of the parts is less likely to be uneven, so that the strain of each part can be suppressed.
進一步,藉由使用石油樹脂及/或石油樹脂衍生物,在 反覆進行金屬材料之熱處理時,可抑制發生的冷卻性能經時性變化。具體而言,在反覆進行金屬材料之熱處理時,可抑制在到達蒸氣膜階段結束之溫度為止的秒數(特性秒數)經時性增加、以及抑制動態黏度經時性低劣。即,藉由使用石油樹脂及/或石油樹脂衍生物,可延長熱處理油組成物之壽命。 Further, by using petroleum resins and/or petroleum resin derivatives, When the heat treatment of the metal material is repeated, the occurrence of the cooling performance over time can be suppressed. Specifically, when the heat treatment of the metal material is repeated, it is possible to suppress the increase in the number of seconds (characteristic seconds) until the temperature at which the vapor film stage is reached, and to suppress the deterioration of the dynamic viscosity with time. That is, the life of the heat-treated oil composition can be prolonged by using a petroleum resin and/or a petroleum resin derivative.
又,藉著石油樹脂及/或石油樹脂衍生物,可縮短熱處理初始階段之特性秒數。 Further, by the petroleum resin and/or the petroleum resin derivative, the number of characteristics in the initial stage of the heat treatment can be shortened.
石油樹脂及/或石油樹脂衍生物之所以可發揮上述效果之理由,推測是因石油樹脂及石油樹脂衍生物的熱塑性特徴、對基油之優異溶解性。 The reason why the petroleum resin and/or the petroleum resin derivative exerts the above effects is presumably due to the thermoplastic properties of the petroleum resin and the petroleum resin derivative, and the excellent solubility to the base oil.
石油樹脂是使選自於石油腦等利用石油類之熱分解行乙烯等烯烴製造時以副產物獲得之碳數4~10之脂肪族烯烴類或脂肪族二烯烴類、或者碳數8以上且具有烯烴性不飽和鍵之芳香族化合物之1種或2種以上之不飽和化合物進行聚合或共聚製得之樹脂。石油樹脂概分為例如使脂肪族烯烴類或脂肪族二烯烴類聚合而成之「脂肪族系石油樹脂」、使具有烯烴性不飽和鍵之芳香族化合物聚合而成之「芳香族系石油樹脂」、使脂肪族烯烴類或脂肪族二烯烴類與具有烯烴性不飽和鍵之芳香族化合物共聚而成之「脂肪族-芳香族共聚石油樹脂」。 The petroleum resin is an aliphatic olefin or an aliphatic diene having a carbon number of 4 to 10 or a carbon number of 8 or more which is obtained by a by-product from the thermal decomposition of petroleum such as petroleum brain. A resin obtained by polymerizing or copolymerizing one or more kinds of unsaturated compounds having an olefinic unsaturated bond. The petroleum resin is, for example, an "aliphatic petroleum resin" obtained by polymerizing an aliphatic olefin or an aliphatic diolefin, and an aromatic petroleum resin obtained by polymerizing an aromatic compound having an olefinic unsaturated bond. An "aliphatic-aromatic copolymerized petroleum resin" obtained by copolymerizing an aliphatic olefin or an aliphatic diolefin with an aromatic compound having an olefinic unsaturated bond.
該碳數4~10之脂肪族烯烴類方面可列舉戊烯、己烯、庚烯等。又,碳數4~10之脂肪族二烯烴類方面可列舉丁二烯、戊二烯、異戊二烯、環戊二烯、二環戊二烯、甲 基戊二烯等。進而,碳數8以上且具有烯烴性不飽和鍵之芳香族化合物方面可列舉苯乙烯、α-甲基苯乙烯、β-甲基苯乙烯、乙烯基甲苯、乙烯基二甲苯、茚、甲基茚、乙基茚等。 Examples of the aliphatic olefin having 4 to 10 carbon atoms include pentene, hexene, heptene and the like. Further, examples of the aliphatic diolefin having 4 to 10 carbon atoms include butadiene, pentadiene, isoprene, cyclopentadiene, dicyclopentadiene, and Kelpene and the like. Further, examples of the aromatic compound having a carbon number of 8 or more and having an olefinic unsaturated bond include styrene, α-methylstyrene, β-methylstyrene, vinyltoluene, vinylxylene, anthracene, and methyl group.茚, ethyl hydrazine, etc.
又,該石油樹脂之原料化合物,不必全部皆為石油腦等利用石油類之熱分解行烯烴製造時之副產物,也可以使用化學合成之不飽和化合物。例如,可舉利用環戊二烯或二環戊二烯之聚合製得之二環戊二烯系石油樹脂、或使該等環戊二烯或二環戊二烯與苯乙烯共聚合而得之二環戊二烯-苯乙烯系石油樹脂。 Further, it is not necessary for all of the raw material compounds of the petroleum resin to be a by-product of the production of olefins by thermal decomposition of petroleum oil such as petroleum brain, and chemically synthesized unsaturated compounds may also be used. For example, a dicyclopentadiene-based petroleum resin obtained by polymerization of cyclopentadiene or dicyclopentadiene or a copolymerization of the cyclopentadiene or dicyclopentadiene with styrene may be used. Dicyclopentadiene-styrene petroleum resin.
石油樹脂衍生物可舉已於上述石油樹脂加成氫原子之氫化石油樹脂。又,石油樹脂衍生物方面可列舉:已將前述石油樹脂利用以羧酸等為代表之酸性官能基予以改質之酸改質石油樹脂、將該酸改質石油樹脂以醇、胺、鹼金屬、鹼土類金屬等化合物予以反應修飾之化合物。 The petroleum resin derivative may be a hydrogenated petroleum resin which has been added to a hydrogen atom of the above petroleum resin. In addition, the petroleum resin derivative may be an acid-modified petroleum resin in which the petroleum resin is modified with an acidic functional group represented by a carboxylic acid or the like, and the acid-modified petroleum resin is an alcohol, an amine or an alkali metal. A compound which is modified by a compound such as an alkaline earth metal.
酸改質石油樹脂大致分為已將石油樹脂以不飽和羧酸、不飽和羧酸酐予以改質之羧酸改質石油樹脂、酸酐改質石油樹脂。不飽和羧酸方面可舉例如丙烯酸、甲基丙烯酸等之不飽和單羧酸類;馬來酸、延胡索酸、依康酸、焦檸檬酸等之不飽和多元羧酸類;馬來酸單甲酯、延胡索酸單乙酯等之不飽和多元羧酸之部分酯類;等,不飽和羧酸酐方面可舉例如馬來酸酐、依康酸酐等之不飽和多元羧酸酐。 The acid-modified petroleum resin is roughly classified into a carboxylic acid-modified petroleum resin and an acid-modified petroleum resin in which a petroleum resin is modified with an unsaturated carboxylic acid or an unsaturated carboxylic anhydride. Examples of the unsaturated carboxylic acid include unsaturated monocarboxylic acids such as acrylic acid and methacrylic acid; unsaturated polycarboxylic acids such as maleic acid, fumaric acid, isoconic acid, and pyrocitric acid; monomethyl maleate and fumaric acid; A partial ester of an unsaturated polycarboxylic acid such as a monoethyl ester; and the unsaturated carboxylic acid anhydride may, for example, be an unsaturated polycarboxylic acid anhydride such as maleic anhydride or isaconic anhydride.
以上述石油樹脂、石油樹脂衍生物而言,脂肪族 -芳香族共聚石油樹脂及氫化脂肪族-芳香族共聚石油樹脂傾向於可縮短特性秒數,在這點上頗為適宜。 In the case of the above petroleum resin and petroleum resin derivative, aliphatic - Aromatic copolymerized petroleum resins and hydrogenated aliphatic-aromatic copolymerized petroleum resins tend to shorten the number of characteristic seconds, which is quite suitable in this regard.
石油樹脂、石油樹脂衍生物之數目平均分子量,從容易發揮本實施形態所獲致之效果這個觀點來看,以200~5000為佳,250~2500較佳,300~1500更佳。 The number average molecular weight of the petroleum resin and the petroleum resin derivative is preferably from 200 to 5,000, more preferably from 250 to 2,500, more preferably from 300 to 1,500, from the viewpoint of easily exerting the effect obtained by the present embodiment.
石油樹脂及/或石油樹脂衍生物,依據JIS K2207:2006環球法所測定之軟化點在40℃以上為佳,60℃以上且150℃以下較佳,80℃以上且140℃以下較佳,85℃以上且130℃以下愈佳。 The petroleum resin and/or petroleum resin derivative preferably has a softening point of 40 ° C or more, 60 ° C or more and 150 ° C or less, preferably 80 ° C or more and 140 ° C or less, in accordance with the method of JIS K2207:2006. Above °C and below 130 °C is better.
藉由使石油樹脂及/或石油樹脂衍生物之軟化點在40℃以上,可使群淬火時各個零件冷卻性能不均(硬度或應變之不均)更不易發生,遇零件為複雜形狀的情況,可使該零件各處冷卻性能不均不易發生,可抑制各零件之應變。 By making the softening point of the petroleum resin and/or petroleum resin derivative above 40 ° C, the uneven cooling performance (hardness or strain unevenness) of each part during group quenching is less likely to occur, and the parts are complicated shapes. The uneven cooling performance of the parts can be prevented from occurring, and the strain of each part can be suppressed.
進一步,藉由使石油樹脂及/或石油樹脂衍生物之軟化點在40℃以上,可更加抑制重複進行熱處理時之冷卻性能經時變化(特性秒數之經時性增加及動態黏度之經時性低劣),同時,可縮短熱處理初始階段時的特性秒數。亦即,藉由使石油樹脂及/或石油樹脂衍生物之軟化點在40℃以上,不僅是初始階段,即使是在重複使用之後,仍可更易於維持熱處理油組成物之冷卻性能,可更長期普遍抑制群淬火時各個零件冷卻性能不均、及各零件之應變。 Further, by making the softening point of the petroleum resin and/or the petroleum resin derivative 40 ° C or more, it is possible to further suppress the change in the cooling performance over time during the repeated heat treatment (the temporal increase of the characteristic number of seconds and the transit time of the dynamic viscosity) Inferiority), at the same time, can shorten the number of characteristic seconds in the initial stage of heat treatment. That is, by making the softening point of the petroleum resin and/or petroleum resin derivative above 40 ° C, it is not only the initial stage, but even after repeated use, the cooling performance of the heat treatment oil composition can be more easily maintained, and Long-term general suppression of uneven quenching performance of each part and quenching of each part.
又,藉由令石油樹脂及/或石油樹脂衍生物之軟化點在150℃以下,可在利用熱處理油組成物將金屬材料等被加工物冷卻之後,減低該被加工物表面之黏膩。 Further, by setting the softening point of the petroleum resin and/or the petroleum resin derivative to 150 ° C or lower, it is possible to reduce the stickiness of the surface of the workpiece after cooling the workpiece such as a metal material with the heat treatment oil composition.
石油樹脂及/或石油樹脂衍生物之軟化點,可依據石油樹脂之聚合程度、改質成分、改質程度來調整。 The softening point of the petroleum resin and/or petroleum resin derivative can be adjusted according to the degree of polymerization, the modified component, and the degree of upgrading of the petroleum resin.
再者,使用二種以上材料來作為石油樹脂及/或石油樹脂衍生物的情況下,所有材料均在上述軟化點範圍為佳。 Further, in the case where two or more materials are used as the petroleum resin and/or the petroleum resin derivative, all of the materials are preferably in the above softening point range.
(B)成分之石油樹脂及/或石油樹脂衍生物相對於熱處理油組成物總量之含有比率,以0.1~90質量%為佳,2~50質量%較佳,5~20質量%更佳。 The content ratio of the petroleum resin and/or petroleum resin derivative of the component (B) to the total amount of the heat-treated oil composition is preferably 0.1 to 90% by mass, preferably 2 to 50% by mass, more preferably 5 to 20% by mass. .
藉由使(B)成分之含有比率在0.1質量%以上,可易於獲得上述之基於(B)成分所達到的效果。又,藉由使(B)成分之含有比率在90質量%以下,可確保負責本質性冷卻性能之(A)成分基油的使用量,可賦予熱處理油組成物冷卻性能。 By setting the content ratio of the component (B) to 0.1% by mass or more, the effect achieved by the above component (B) can be easily obtained. In addition, when the content ratio of the component (B) is 90% by mass or less, the amount of the component (A) component oil which is responsible for the essential cooling performance can be ensured, and the heat treatment oil composition can be provided with cooling performance.
合計(A)成分及(B)成分之含量,相對於熱處理油組成物總量計,以80質量%以上為佳,90質量%以上較佳,100質量%更佳。 The content of the component (A) and the component (B) is preferably 80% by mass or more, more preferably 90% by mass or more, and still more preferably 100% by mass based on the total amount of the heat-treated oil composition.
又,只要是在不阻礙本實施形態效果的範圍,熱處理油組成物中也可含有石樹脂及/或石油樹脂衍生物以外的蒸氣膜破裂劑。其他蒸氣膜破裂劑可舉萜烯樹脂、萜烯樹脂衍生物、松香、松香衍生物等。 Further, the heat treatment oil composition may contain a vapor film breaker other than the stone resin and/or the petroleum resin derivative as long as it does not inhibit the effects of the embodiment. Other vapor film breakers include terpene resins, terpene resin derivatives, rosins, and rosin derivatives.
[(C)添加劑] [(C) Additives]
本實施形態之熱處理油組成物,可含有抗氧化劑、冷卻性能提升劑等添加劑。 The heat-treated oil composition of the present embodiment may contain an additive such as an antioxidant or a cooling performance enhancer.
抗氧化劑、冷卻性能提升劑等之含有比率,相對於熱處理油組成物總量,各自以10質量%以下為佳,0.01~5質量%較佳。 The content ratio of the antioxidant, the cooling performance enhancer, and the like is preferably 10% by mass or less, and preferably 0.01 to 5% by mass based on the total amount of the heat-treated oil composition.
[熱處理油組成物之物性] [The physical properties of the heat-treated oil composition]
本實施形態之熱處理油組成物,由冷卻曲線獲得之特性秒數必須在1.00秒以下,該冷卻曲線是依循JIS K2242:2012之冷卻性能測試方法求得。 In the heat-treated oil composition of the present embodiment, the number of characteristics obtained from the cooling curve must be 1.00 second or less, and the cooling curve is obtained in accordance with the cooling performance test method of JIS K2242:2012.
熱處理油組成物之特性秒數若超過1.00秒,會變得難以降低群淬火時各個零件冷卻性能不均,又,也變得難以抑制各零件之應變。 When the number of seconds of the heat treatment oil composition exceeds 1.00 second, it becomes difficult to reduce unevenness in cooling performance of each part during quenching, and it is also difficult to suppress the strain of each part.
熱處理油組成物之特性秒數以0.95秒以下為佳,0.90秒以下較佳。 The number of seconds of the characteristic of the heat-treating oil composition is preferably 0.95 seconds or less, more preferably 0.90 second or less.
更具體而言,特性秒數是依據以下(1)、(2)算出。 More specifically, the number of characteristic seconds is calculated based on the following (1) and (2).
(1)依循JIS K2242:2012冷卻性能測試方法,將以加熱至810℃之銀試料投入於熱處理油組成物,求出以時間為x軸、以該銀試料表面溫度為y軸之冷卻曲線。 (1) According to the cooling performance test method of JIS K2242:2012, a silver sample heated to 810 ° C was placed in a heat treatment oil composition, and a cooling curve in which the time was the x-axis and the surface temperature of the silver sample was the y-axis was obtained.
(2)依據切線交叉法,由前述冷卻曲線算出到達熱處理油組成物之蒸氣膜階段結束的溫度(特性溫度)為止的秒數,以該秒數為特性秒數。 (2) The number of seconds until the temperature (characteristic temperature) at which the vapor film stage of the heat treatment oil composition ends is calculated from the tangential intersection method, and the number of seconds is the characteristic second.
又,上述(1)中,測定時間之間隔定為1/100秒為佳。 Further, in the above (1), the interval between the measurement times is preferably 1/100 second.
進而,本實施形態之熱處理油組成物,冷卻曲線從800℃起至300℃為止之冷卻時間即「300℃秒數」必須在6.00秒以上且14.50秒以下,該冷卻曲線係依循JIS K2242:2012之冷卻性能測試方法而求得。 Further, in the heat-treated oil composition of the present embodiment, the cooling time of the cooling curve from 800 ° C to 300 ° C, that is, "300 ° C seconds" must be 6.00 seconds or more and 14.50 seconds or less, and the cooling curve is in accordance with JIS K2242:2012. The cooling performance test method is obtained.
熱處理油組成物之300℃秒數一旦脫離上述範圍,欲使熱處理油組成物之冷卻性能與JIS K2242:2012之2種1號油相同程度就變得有困難。 When the number of seconds of 300 ° C of the heat-treated oil composition is out of the above range, it is difficult to make the cooling performance of the heat-treated oil composition the same as that of the two types of No. 1 oil of JIS K2242:2012.
熱處理油組成物之300℃秒數,以6.50~13.50秒為佳,7.00~12.50秒較佳。 The heat treatment oil composition has a number of 300 ° C seconds, preferably 6.50 to 13.50 seconds, and preferably 7.00 to 12.50 seconds.
為了使熱處理油組成物之特性秒數及300℃秒數在上述範圍,以令(A)成分之含量及40℃動態黏度、以及(B)成分之含量、軟化點及數目平均分子量在上述實施形態範圍內為佳。 In order to make the characteristic number of seconds of the heat-treated oil composition and the number of seconds of 300 ° C in the above range, the content of the component (A) and the dynamic viscosity at 40 ° C, and the content of the component (B), the softening point and the number average molecular weight are carried out as described above. It is better within the range of morphology.
本實施形態之熱處理油組成物,100℃動態黏度以10~30mm2/s為佳,15~20mm2/s較佳。 In the heat-treated oil composition of the present embodiment, the dynamic viscosity at 100 ° C is preferably 10 to 30 mm 2 /s, and preferably 15 to 20 mm 2 /s.
接著,依據實施例進一步詳細說明本發明,不過本發明並不因該等例而受任何限定。 Next, the present invention will be described in further detail based on examples, but the present invention is not limited by the examples.
A.評估、測定 A. Evaluation, measurement
A-1.硬度及應變 A-1. Hardness and strain
淬火評估用材料係使用圓筒形狀之膚鍛鋼(外徑φ85mm、高度44mm、厚度4mm、材質SCM415),依下述條件進行熱處理等,進一步,針對下述項目進行評估。 For the quenching evaluation material, a cylindrical forged steel (outer diameter φ85 mm, height 44 mm, thickness 4 mm, material SCM415) was used, and heat treatment was performed under the following conditions, and further, the following items were evaluated.
<熱處理等條件> <conditions such as heat treatment>
熱處理條件:滲碳步驟930℃×150分、CP(碳位能)=1.1質量% Heat treatment conditions: carburization step 930 ° C × 150 minutes, CP (carbon potential energy) = 1.1% by mass
擴散步驟:930℃×60分、CP(碳位能)=0.8質量% Diffusion step: 930 ° C × 60 minutes, CP (carbon energy) = 0.8% by mass
均熱步驟:850℃×20分、CP(碳位能)=0.8質量% Soaking step: 850 ° C × 20 minutes, CP (carbon energy) = 0.8% by mass
油冷條件:油溫120℃、油冷時間10分、攪拌20Hz Oil cooling conditions: oil temperature 120 ° C, oil cooling time 10 minutes, stirring 20 Hz
回火條件:180℃×60分 Tempering conditions: 180 ° C × 60 minutes
安置方法:刀架(淬火架8個,4個×2段) Placement method: knife holder (8 quenching frames, 4 x 2 segments)
<評估項目> <evaluation project>
‧平均橢圓率(mm) ‧ average ellipticity (mm)
‧橢圓率3 σ(mm) ‧Ellipticity rate 3 σ(mm)
‧平均錐度應變(mm) ‧ average taper strain (mm)
‧錐度應變3 σ(mm) ‧ taper strain 3 σ (mm)
‧平均內部硬度(淬火材料1.5mm內部、HV) ‧ Average internal hardness (1.5mm internal quenching material, HV)
‧平均有效硬化層深度(mm) ‧ average effective hardened layer depth (mm)
A-2.初始冷卻性能 A-2. Initial cooling performance
依循JIS K2242:2012所規定之冷卻性能測試方法,將已加熱至810℃之銀試料投入至熱處理油組成物,求取銀試料之冷卻曲線,算出以下「特性秒數」及「300℃秒數」。銀試料投入前熱處理油組成物之油溫,實施例1-1~1-9、比較例1、實施例2及比較例2-1~2-2均定為120℃。 According to the cooling performance test method specified in JIS K2242:2012, the silver sample heated to 810 ° C is put into the heat treatment oil composition, and the cooling curve of the silver sample is obtained, and the following "characteristic seconds" and "300 ° C seconds are calculated. "." The oil temperature of the oil composition before the injection of the silver sample was carried out, and Examples 1-1 to 1-9, Comparative Example 1, Example 2, and Comparative Examples 2-1 to 2-2 were each set to 120 °C.
<特性秒數> <characteristic seconds>
上述冷卻曲線中,依循JIS K2242:2012,算出蒸氣膜階段結束之溫度(特性溫度),以到達該溫度為止的秒數為特性秒數。 In the above cooling curve, the temperature (characteristic temperature) at which the vapor film stage is completed is calculated in accordance with JIS K2242:2012, and the number of seconds until the temperature is reached is the characteristic second.
<300℃秒數> <300°C seconds>
上述冷卻曲線中令從800℃起至300℃為止之冷卻時間為300℃秒數。 In the above cooling curve, the cooling time from 800 ° C to 300 ° C is 300 ° C.
A-3.冷卻性能之經時穩定性 A-3. Stability over time of cooling performance
以上述A-2之結果為重複淬火劣化測試前之結果。接著,依以下所示條件進行重複淬火劣化測試。該劣化測試後,再次重新進行與上述A-2同樣的測試及評估,以其為重 複淬火劣化測試後之結果。依據以下式(2),算出測試前後之變化率。 The result of the above A-2 is the result before the repeated quenching deterioration test. Next, the repeated quenching deterioration test was performed under the conditions shown below. After the deterioration test, the same test and evaluation as A-2 above is repeated again, with the emphasis on The result after the quenching deterioration test. The rate of change before and after the test was calculated according to the following formula (2).
[(測試後之值-測試前之值)/測試前之值]×100 (2) [(value after test - value before test) / value before test] × 100 (2)
<測試條件> <test conditions>
測試片:SUS316 Test piece: SUS316
淬火溫度:850℃ Quenching temperature: 850 ° C
油量:400ml Oil quantity: 400ml
油溫:170℃ Oil temperature: 170 ° C
淬火次數:400回 Quenching times: 400 times
A-4.動態黏度 A-4. Dynamic viscosity
依循JIS K2283:2000,於上述A-3之重複淬火劣化測試前後測定熱處理油組成物之100℃動態黏度。 The 100 ° C dynamic viscosity of the heat-treated oil composition was measured before and after the repeated quenching deterioration test of A-3 in accordance with JIS K2283:2000.
B.熱處理油組成物之調製及評估 B. Modulation and evaluation of heat treatment oil composition
(實施例1-1~1-9、比較例1) (Examples 1-1 to 1-9, Comparative Example 1)
調製表1之組成之熱處理油組成物,進行上述A-2及A-4之評估以及測定。結果顯示於表1。 The heat-treated oil composition of the composition of Table 1 was prepared, and the evaluation and measurement of the above A-2 and A-4 were carried out. The results are shown in Table 1.
表1之材料如下。 The materials in Table 1 are as follows.
基油1:40℃動態黏度90mm2/s之礦油 Base oil 1:40 ° C dynamic viscosity 90mm 2 / s mineral oil
石油1-1:部分氫化脂肪族-芳香族共聚石油樹脂、軟化點110℃、數目平均分子量760 Petroleum 1-1: partially hydrogenated aliphatic-aromatic copolymerized petroleum resin, softening point 110 ° C, number average molecular weight 760
石油1-2:脂肪族石油樹脂、軟化點99℃、數目平均分子量1300 Oil 1-2: aliphatic petroleum resin, softening point 99 ° C, number average molecular weight 1300
石油1-3:脂肪族-芳香族共聚石油樹脂、軟化點103℃、數目平均分子量900 Petroleum 1-3: aliphatic-aromatic copolymerized petroleum resin, softening point 103 ° C, number average molecular weight 900
石油1-4:氫化脂肪族石油樹脂、軟化點105℃、數目平均分子量400 Petroleum 1-4: hydrogenated aliphatic petroleum resin, softening point 105 ° C, number average molecular weight 400
石油1-5:氫化脂肪族石油樹脂、軟化點125℃、數目平均分子量430 Petroleum 1-5: hydrogenated aliphatic petroleum resin, softening point 125 ° C, number average molecular weight 430
石油1-6:氫化脂肪族石油樹脂、軟化點87℃、數目平均分子量370 Petroleum 1-6: hydrogenated aliphatic petroleum resin, softening point 87 ° C, number average molecular weight 370
石油1-7:氫化脂肪族石油樹脂、軟化點103℃、數目 平均分子量410 Petroleum 1-7: hydrogenated aliphatic petroleum resin, softening point 103 ° C, number Average molecular weight 410
石油1-8:部分氫化芳香族改質脂肪族石油樹脂、軟化點102℃、數目平均分子量500 Petroleum 1-8: partially hydrogenated aromatic modified aliphatic petroleum resin, softening point 102 ° C, number average molecular weight 500
石油1-9:脂肪族石油樹脂、軟化點124℃、數目平均分子量430 Petroleum 1-9: aliphatic petroleum resin, softening point 124 ° C, number average molecular weight 430
由表1之結果可清楚確認,實施例1-1~1-9之熱處理油組成物,300℃秒數短,具有與JIS K2242:2012之2種1號油相同程度之冷卻性能。 As is clear from the results of Table 1, the heat-treated oil compositions of Examples 1-1 to 1-9 had a short cycle time of 300 ° C and had the same degree of cooling performance as the two types of No. 1 oil of JIS K2242:2012.
又,實施例1-1~1-9之熱處理油組成物,可確認特性秒數很短。因此可知,當使用實施例1-1~1-9之熱處理油組成物時,抑制群淬火時各個零件冷卻性能不均、抑制各零件之應變可期。 Further, in the heat-treated oil compositions of Examples 1-1 to 1-9, it was confirmed that the characteristic number of seconds was short. Therefore, it is understood that when the heat-treating oil compositions of Examples 1-1 to 1-9 are used, it is possible to suppress unevenness in cooling performance of each part during quenching of the group and to suppress strain of each part.
(實施例2、比較例2-1~2-2) (Example 2, Comparative Example 2-1 to 2-2)
調製表2之組成之熱處理油組成物,進行上述A-1~A-4之測定及評估。 The heat treatment oil composition of the composition of Table 2 was prepared, and the measurement and evaluation of the above A-1 to A-4 were carried out.
又,上述A-4之100℃動態黏度,是在上述A-3重複淬火劣化測試前後進行測定。結果顯示於表2。 Further, the dynamic viscosity at 100 ° C of the above A-4 was measured before and after the above-mentioned A-3 repeated quenching deterioration test. The results are shown in Table 2.
表2之材料如下。 The materials in Table 2 are as follows.
基油2-1:40℃動態黏度120mm2/s之礦油 Base oil 2-1: 40 ° C dynamic viscosity 120mm 2 / s mineral oil
基油2-2:40℃動態黏度60mm2/s之礦油 Base oil 2-2: 40 ° C dynamic viscosity 60 mm 2 / s mineral oil
基油2-3:40℃動態黏度200mm2/s之礦油 Base oil 2-3:40 °C dynamic viscosity 200mm 2 / s mineral oil
石油樹脂2:部分氫化脂肪族-芳香族共聚石油樹脂、軟化點110℃、數目平均分子量760 Petroleum Resin 2: partially hydrogenated aliphatic-aromatic copolymerized petroleum resin, softening point 110 ° C, number average molecular weight 760
α烯烴共聚物:100℃動態黏度2000mm2/s之α烯烴共 聚物 Alpha olefin copolymer: α-olefin copolymer with dynamic viscosity of 2000 mm 2 /s at 100 ° C
由表2之結果可清楚確認,實施例2之熱處理油組成物,300℃秒數短,具有與JIS K2242:2012之2種1號油相同程度之冷卻性能。又,實施例2之熱處理油組成物,橢圓率3 σ及錐度應變3 σ之值很小,確認可抑制群淬火時應變之不均。進而確認,實施例2之熱處理油組成物可抑制在進行重複熱處理時之經時性性能劣化(特性秒數增加、300℃秒數增加、動態黏度減少)。 As is clear from the results of Table 2, the heat-treated oil composition of Example 2 had a short cycle time of 300 ° C and had the same degree of cooling performance as the two types of No. 1 oil of JIS K2242:2012. Further, in the heat-treated oil composition of Example 2, the values of the ellipticity 3 σ and the taper strain 3 σ were small, and it was confirmed that the strain unevenness during group quenching can be suppressed. Further, it was confirmed that the heat-treated oil composition of Example 2 can suppress deterioration of the temporal property at the time of performing the repeated heat treatment (increased number of characteristics, increased number of seconds at 300 ° C, and reduced dynamic viscosity).
又確認,實施例2之熱處理油組成物,初始階段之特性秒數及300℃秒數顯示出極佳之值,從初始階段起涵蓋重複使用後之長期間均可維持良好性能。 Further, it was confirmed that the heat-treated oil composition of Example 2 exhibited an excellent value in the number of seconds of the initial stage and the number of seconds at 300 ° C, and maintained good performance from the initial stage to the long period after repeated use.
本實施形態之熱處理油組成物可維持與JIS K2242:2012之2種1號油相同程度之冷卻性能卻又可減低群淬火時各個零件冷卻性能不均,同時可抑制重複進行金屬材料熱處理時發生的冷卻性能經時變化。因此,本實施形態之熱處理油組成物,可適當作為對含碳鋼、鎳-錳鋼、鉻-鉬鋼、錳鋼等合金鋼施行淬火、退火、回火等熱處理時的熱處理油來使用,尤其,其中又以作為進行淬火時的熱處理油來使用為適宜。 The heat-treated oil composition of the present embodiment can maintain the same degree of cooling performance as the two types of No. 1 oil of JIS K2242:2012, but can also reduce the unevenness of cooling performance of each part during group quenching, and can suppress occurrence of repeated heat treatment of the metal material. The cooling performance changes over time. Therefore, the heat-treated oil composition of the present embodiment can be suitably used as a heat-treated oil for heat treatment such as quenching, annealing, tempering, or the like on alloy steels such as carbon-containing steel, nickel-manganese steel, chromium-molybdenum steel, and manganese steel. In particular, it is suitable to use it as a heat treatment oil at the time of quenching.
Claims (6)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2015030026A JP6569145B2 (en) | 2015-02-18 | 2015-02-18 | Heat treated oil composition |
JP2015-030026 | 2015-02-18 |
Publications (2)
Publication Number | Publication Date |
---|---|
TW201634682A true TW201634682A (en) | 2016-10-01 |
TWI681051B TWI681051B (en) | 2020-01-01 |
Family
ID=56692096
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW105103121A TWI681051B (en) | 2015-02-18 | 2016-02-01 | Heat treatment oil composition |
Country Status (5)
Country | Link |
---|---|
US (1) | US20180023021A1 (en) |
JP (1) | JP6569145B2 (en) |
CN (1) | CN107250389A (en) |
TW (1) | TWI681051B (en) |
WO (1) | WO2016132860A1 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6355033B1 (en) * | 2017-08-22 | 2018-07-11 | 大同化学工業株式会社 | Water-soluble heat treatment composition |
CN111868269A (en) * | 2018-03-28 | 2020-10-30 | 出光兴产株式会社 | Heat treatment oil composition |
US20210009917A1 (en) * | 2018-03-28 | 2021-01-14 | Idemitsu Kosan Co.,Ltd. | Heat-treatment oil composition |
CN111560498B (en) * | 2020-06-08 | 2021-12-24 | 马鞍山常裕机械设备有限公司 | High-temperature isothermal quenching process for high-chromium alloy casting grinding ball |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3567640A (en) * | 1970-03-25 | 1971-03-02 | Park Chem Co | Quench oil composition and method of use |
US3681150A (en) * | 1970-05-25 | 1972-08-01 | Exxon Research Engineering Co | Fast cold quench oil for metals |
US3855014A (en) * | 1973-06-25 | 1974-12-17 | Atlantic Richfield Co | Quenching oil composition and method of quenching metal |
JP4659264B2 (en) * | 2001-05-02 | 2011-03-30 | 出光興産株式会社 | Heat treated oil composition |
CA2470323A1 (en) * | 2001-12-18 | 2003-06-26 | The Lubrizol Corporation | Quenching oil compositions |
JP4764336B2 (en) * | 2004-03-10 | 2011-08-31 | 出光興産株式会社 | Quenching oil for quenching under reduced pressure and quenching method |
JP4691405B2 (en) * | 2005-06-28 | 2011-06-01 | 出光興産株式会社 | Heat treated oil composition |
JP5642327B2 (en) * | 2006-11-15 | 2014-12-17 | 株式会社三ツ知春日井 | Hardening method for steel |
JP5253772B2 (en) * | 2007-07-27 | 2013-07-31 | 出光興産株式会社 | Heat treated oil composition |
CN102021280B (en) * | 2011-01-07 | 2012-05-30 | 山东卡松科技有限公司 | Heat treating oil and preparation method thereof |
CN102212662B (en) * | 2011-06-09 | 2012-10-03 | 上海德润宝特种润滑剂有限公司 | Ultra quick quenching oil and preparation method thereof |
JP5809088B2 (en) * | 2012-03-16 | 2015-11-10 | 出光興産株式会社 | Heat treated oil composition |
JP5930981B2 (en) * | 2013-02-06 | 2016-06-08 | 出光興産株式会社 | Heat treated oil composition |
-
2015
- 2015-02-18 JP JP2015030026A patent/JP6569145B2/en active Active
-
2016
- 2016-01-29 US US15/550,973 patent/US20180023021A1/en not_active Abandoned
- 2016-01-29 CN CN201680010378.7A patent/CN107250389A/en active Pending
- 2016-01-29 WO PCT/JP2016/052632 patent/WO2016132860A1/en active Application Filing
- 2016-02-01 TW TW105103121A patent/TWI681051B/en active
Also Published As
Publication number | Publication date |
---|---|
JP2016151054A (en) | 2016-08-22 |
CN107250389A (en) | 2017-10-13 |
US20180023021A1 (en) | 2018-01-25 |
JP6569145B2 (en) | 2019-09-04 |
WO2016132860A1 (en) | 2016-08-25 |
TWI681051B (en) | 2020-01-01 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TW201634682A (en) | Heat treatment oil composition | |
KR101186698B1 (en) | Quenching oil for reduced pressure quenching and method for quenching | |
JP4691405B2 (en) | Heat treated oil composition | |
JP5930981B2 (en) | Heat treated oil composition | |
TWI675911B (en) | Heat treatment oil composition | |
CN110747319B (en) | Overspeed quenching oil and preparation method thereof | |
JP5809088B2 (en) | Heat treated oil composition | |
JP4659264B2 (en) | Heat treated oil composition | |
CN109022713A (en) | Emulsion resistance type quenching oil compound and application thereof | |
CN111471842A (en) | Over-speed bright quenching oil with stable cooling speed | |
KR20160070305A (en) | Steel material for graphitization and graphite steel with excellent machinability and cold forging characteristic | |
TWI805724B (en) | Heat Treatment Oil Composition | |
TW201945528A (en) | Heat-treatment oil composition | |
JP2010209422A (en) | Heat treatment oil composition | |
JP2854399B2 (en) | Rubber composition |