KR100262884B1 - Operating oil of power type direction regulator for automobile - Google Patents

Operating oil of power type direction regulator for automobile Download PDF

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Publication number
KR100262884B1
KR100262884B1 KR1019970044757A KR19970044757A KR100262884B1 KR 100262884 B1 KR100262884 B1 KR 100262884B1 KR 1019970044757 A KR1019970044757 A KR 1019970044757A KR 19970044757 A KR19970044757 A KR 19970044757A KR 100262884 B1 KR100262884 B1 KR 100262884B1
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South Korea
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oil
unconverted
weight
distillation process
base oil
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KR1019970044757A
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Korean (ko)
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KR19990021229A (en
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박주천
양시원
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남창우
에스케이주식회사
정몽규
현대자동차주식회사
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Priority to KR1019970044757A priority Critical patent/KR100262884B1/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B62LAND VEHICLES FOR TRAVELLING OTHERWISE THAN ON RAILS
    • B62DMOTOR VEHICLES; TRAILERS
    • B62D5/00Power-assisted or power-driven steering
    • B62D5/06Power-assisted or power-driven steering fluid, i.e. using a pressurised fluid for most or all the force required for steering a vehicle
    • B62D5/07Supply of pressurised fluid for steering also supplying other consumers ; control thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G65/00Treatment of hydrocarbon oils by two or more hydrotreatment processes only
    • C10G65/02Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only
    • C10G65/12Treatment of hydrocarbon oils by two or more hydrotreatment processes only plural serial stages only including cracking steps and other hydrotreatment steps
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G7/00Distillation of hydrocarbon oils
    • C10G7/06Vacuum distillation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G71/00Treatment by methods not otherwise provided for of hydrocarbon oils or fatty oils for lubricating purposes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M171/00Lubricating compositions characterised by purely physical criteria, e.g. containing as base-material, thickener or additive, ingredients which are characterised exclusively by their numerically specified physical properties, i.e. containing ingredients which are physically well-defined but for which the chemical nature is either unspecified or only very vaguely indicated
    • C10M171/02Specified values of viscosity or viscosity index
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60YINDEXING SCHEME RELATING TO ASPECTS CROSS-CUTTING VEHICLE TECHNOLOGY
    • B60Y2306/00Other features of vehicle sub-units
    • B60Y2306/09Reducing noise
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/08Hydraulic fluids, e.g. brake-fluids

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Transportation (AREA)
  • Mechanical Engineering (AREA)
  • Lubricants (AREA)

Abstract

PURPOSE: Lubricating oil of a power steering device is provided to reduce noises occurring in sliding parts of a power steering by using actuating oil of low frictional coefficient. CONSTITUTION: A hydrogenation decomposition process comprises an atmospheric pressure sediment oil distillation process, a decompression gas oil hydrogenation process, a decompression gas oil hydrogenation decomposition reactive process and fractional distillation process. Unconverted oil is recycled from the fractional distillation process to the decompression distillation process of atmospheric pressure sediment oil in a fuel oil hydrogenation decomposition process of recycle mode. Herein, a part or all of unconverted oil is sent to the unconverted oil decompression distillation process to be manufactured and containing a viscosity of 3¯8 centistoke at 100deg.C and high level lubricating oil of over 100 of viscosity. Rest of unconverted oil is recycled only to the decompression gas oil hydrogenation process.

Description

자동차용 동력식 조향장치의 작동유Hydraulic fluid for motorized steering

본 발명은 자동차용 동력식 조향장치에 사용되는 작동유에 관한 것으로서, 더욱 상세하게는 특정의 생산 공정에 의하여 제조된 고급윤활기유를 포함하는 동력식 조향장치의 작동유에 관한 것이다. 본 발명의 동력식 조향장치의 작동유은 마찰계수가 낮으므로 조향장치내 각종 습동부에서 발생할 수 있는 소음을 감소시킨다.The present invention relates to hydraulic fluid used in motorized steering apparatus for automobiles, and more particularly, to hydraulic oil of a motorized steering apparatus including high-grade lubricant base oil produced by a specific production process. The hydraulic fluid of the power steering apparatus of the present invention has a low coefficient of friction, thereby reducing noise that may occur in various sliding parts in the steering apparatus.

자동차의 주행성능과 편리함 등을 위하여 동력식 조향장치의 장착이 확대되어 근래 승용차의 95% 이상이 동력식 조향장치를 장착하고 있으며, 한층 기능도 복잡해져, 회전수 감응식 조향장치, 속도 감응식 조향장치 등 다양한 형태의 동력식 조향장치가 개발되어 사용되고 있다. 이러한 동력식 조향장치는 베인펌프나 기어펌프와 같은 유압펌프에 의해 압력을 발생시켜 이 압력을 이용해 조향을 하는 것으로 여기에 사용되는 윤활유는 유압발생 및 피스톤과 실린더사이, 기어펌프의 기어와 기어사이 또는 베인펌프의 베인과 링사이 등의 윤활을 담당하고 있으므로 통상적으로 적정한 점도 특성, 우수한 저온유동성, 내마모성, 마찰특성, 열산화 안정성, 내소부성, 고무재와의 적합성 및 소포성과 같은 특성들이 요구되고 있다.The motorized steering system has been expanded for the driving performance and convenience of the vehicle. More than 95% of passenger cars are equipped with the power steering system, and the functions are further complicated, and the speed-sensitive steering system and the speed-sensitive steering system are also complicated. Various types of power steering devices, such as devices, have been developed and used. Such a power steering system generates pressure by a hydraulic pump such as a vane pump or a gear pump to steer using this pressure. The lubricant used is between a hydraulic generation and a piston and a cylinder, and a gear and a gear of a gear pump. Or it is in charge of the lubrication between the vane and the vane of the vane pump, so the characteristics such as proper viscosity characteristics, excellent low temperature fluidity, abrasion resistance, friction characteristics, thermal oxidation stability, seizure resistance, compatibility with rubber materials and antifoaming properties are usually required. have.

그러나 종래 동력식 조향장치 작동유는 펌프 습동부나 밸브에서의 마찰계수가 높다는 문제점을 가지고 있으며, 이러한 마찰특성은 습동부로부터 소음을 야기시켜 동력식 조향장치의 정숙성을 떨어뜨리게 한다.However, the conventional power steering hydraulic fluid has a problem that the coefficient of friction in the pump sliding part or the valve is high, and such friction characteristics cause noise from the sliding part to reduce the quietness of the power steering device.

상기와 같은 문제점을 해결하기 위해 일본특허 특개평 5-331477에서는 티오인산아연, 아인산에스테르 및 인산에스테르를 적어도 1종 이상 사용하고 글리세린 지방산에스테르를 사용하여 이러한 문제점을 개선하였고, 일본특허 특개평 5-125383에서는 중량평균분자량이 10만 이상의 올레핀코폴리머 또는 폴리이소부틸렌을 적용하여 이러한 문제를 개선하였다. 한편, 저마찰계수를 실현하기 위해 과다한 마찰저감첨가제를 사용함으로써 안정성이 떨어져 첨가제가 침강하는 문제점이 야기되기도 하는 데, 일본특허 특개평 2-265998에서는 이러한 문제점을 용해성이 우수한 기유를 적용하여 개선하고자 하였다. 그러나 상기와 같은 방법들은 저마찰계수를 실현하기 위해 마찰저감첨가제를 사용하고, 이러한 첨가제들의 용해도를 높이기 위해 용해성이 높은 기유를 사용하는 방법들로 기유자체가 갖는 마찰특성을 고려하지 않고 있다.In order to solve the above problems, Japanese Patent Laid-Open Publication No. 5-331477 uses at least one type of zinc thiophosphate, phosphite ester and phosphate ester and improves these problems by using glycerin fatty acid ester. In 125383, a weight average molecular weight of 100,000 or more olefin copolymers or polyisobutylenes was applied to alleviate this problem. On the other hand, by using an excessive friction reducing additive to realize a low friction coefficient, there is also a problem that the additives settle down due to poor stability, Japanese Patent Laid-Open No. 2-265998 is to improve this problem by applying a base oil having excellent solubility It was. However, the above methods do not consider the friction characteristics of the base oil itself by using a friction reducing additive to realize a low friction coefficient and using a high solubility base oil to increase the solubility of these additives.

이에, 본 발명자는 기유 자체가 갖는 마찰특성을 주목하여 특정의 생산공정으로 생산한 기유가 저마찰특성을 실현하는데 있어 일반의 상용공정으로 생산된 기유보다 우수하다는 사실을 알고, 이를 동력식 조향장치 작동유에 적용, 마찰계수가 낮은 작동유인 본 발명을 완성하였다.Accordingly, the present inventors pay attention to the friction characteristics of the base oil itself, and know that the base oil produced by a specific production process is superior to the base oil produced by a common commercial process in realizing low friction characteristics, and this is a power steering device Applied to the hydraulic fluid, the present invention has been completed, which is a hydraulic fluid having a low coefficient of friction.

본 발명은 동력식 조향장치내 각종 습동부에서 발생할 수 있는 소음을 감소시키기 위하여 마찰계수가 낮은 동력식 조향장치의 작동유을 제공하는 것을 목적으로 한다.An object of the present invention is to provide a hydraulic oil of a power steering device with a low friction coefficient in order to reduce noise that may occur in various sliding parts in the power steering device.

상기 목적을 달성하기 위하여, 본 발명의 동력식 조향장치의 작동유는 상압 잔사유 감압증류 공정, 감압 가스유 수소화 처리반응 공정, 감압 가스유 수소화분해반응 공정 및 분별증류 공정으로 구성된 수소화 분해공정에서 미전환유(UCO)를 분별증류 공정으로부터 상압잔사유 감압증류 공정으로 리사이클시키는 공정으로 구성된 리사이클 모드의 연료유 수소화 분해 공정에 있어서, 상기 미전환유의 일부 또는 전부를 별도의 미전환유 감압증류 공정으로 보내서 제조되는, 점도가 100℃에서 3 내지 8 센티스톡이고, 점도지수가 100 이상인 고급 윤활기유를 포함한다. 여기에서 상기 미전환유의 나머지는 상기 감압가스유 수소화 분해 공정으로만 리사이클시킨다.In order to achieve the above object, the operating oil of the power steering apparatus of the present invention is undiluted in the hydrocracking process consisting of atmospheric residue oil pressure distillation process, vacuum gas oil hydroprocessing reaction process, vacuum gas oil hydrocracking reaction process and fractional distillation process. In a fuel oil hydrocracking process of a recycled mode consisting of recycling oil (UCO) from a fractional distillation process to a vacuum residue distillation process, a part or all of the unconverted oil is sent to a separate unconverted oil vacuum distillation process. It includes a high lubricating base oil having a viscosity of 3 to 8 centistokes at 100 ° C. and a viscosity index of 100 or more. Here, the remainder of the unconverted oil is recycled only to the vacuum gas hydrocracking process.

상기 미전환유 감압증류 공정에 있어서, 미전환유중 상기의 점도등급의 미전환유는 수소화 탈왁스 및 안정화 공정으로 진행되며, 나머지 미전환유는 감압가스유 수소화 분해반응 공정으로 리사이클된다. 또한 상기 미전환유 감압증류 공정은 탑저 온도기준 300 내지 350℃의 온도 및 50 내지 300mmHg의 탑저 압력으로 운전된다.In the unconverted oil vacuum distillation process, the unconverted oil having the above viscosity grade in the unconverted oil is subjected to a hydrodeswaxing and stabilization process, and the remaining unconverted oil is recycled to a reduced pressure gas oil hydrocracking reaction process. In addition, the unconverted oil vacuum distillation process is operated at a temperature of 300 to 350 ° C. and a bottom pressure of 50 to 300 mmHg.

또한, 상기 고급 윤활기유는 나프텐 성분 55 내지 75중량%, 파라핀 성분 40 내지 25중량% 및 방향족 성분 0 내지 5중량%로 구성된다.In addition, the higher lubricating base oil is composed of 55 to 75% by weight naphthene component, 40 to 25% by weight paraffin component and 0 to 5% by weight aromatic component.

상기 고급 윤활기유를 이용하여 동력식 조향장치의 작동유로 사용할 경우, 사용되는 양은 중량 퍼센트를 기준으로 100중량%로서 즉, 고급 윤활기유 단독으로 작동유로 사용될 수 있으며, 또한, 상기 고급 윤활기유와 타종의 기유 예를 들어 용제추출법 광유계 기유, 수첨개질법 광유계 기유와 같은 일반적인 광유계 기유나 폴리알파올레핀, 폴리올에스테르 또는 디베이직에스테르 등의 합성 기유를 혼합하여 작동유로 사용할 수 있다. 상기의 고급 윤활기유를 타종의 기유와 혼합하여 사용할 경우, 상기 고급 윤활기유를 중량 퍼센트 기준으로 10중량% 이상, 바람직하게는 50 내지 80중량% 사용한다. 상기 고급 윤활기유가 10중량% 이하인 경우에는 상기 고급 윤활기유가 갖는 장점이 발휘되기 어렵다.When used as the hydraulic oil of the power steering device using the high-grade lubricant base oil, the amount used is 100% by weight based on the weight percent, that is, the high-grade lubricant base oil can be used as the operating oil alone, and also the other high-grade lubricant base oil For example, the base oil may be mixed with a general mineral oil base oil such as solvent extraction mineral oil base oil, hydrogenation reforming mineral oil base oil or synthetic base oils such as polyalphaolefin, polyol ester or dibasic ester may be used as a working oil. When the higher lubricating base oil is mixed with other base oils, the higher lubricating base oil is used in an amount of 10% by weight or more, preferably 50 to 80% by weight. When the higher lubricating base oil is 10% by weight or less, the advantages of the high lubricating base oil are hardly exhibited.

이하, 실시예에 의하여 본 발명을 더욱 상세하게 설명한다. 그러나 하기 실시예는 본 발명의 예시일 뿐이므로 하기 실시예에 의하여 본 발명이 한정되는 것으로 간주되어서는 안된다.Hereinafter, the present invention will be described in more detail with reference to Examples. However, the following examples are only illustrative of the present invention and the present invention should not be considered as being limited by the following examples.

〈실시예 1〉 고급 윤활기유의 제조<Example 1> Preparation of high grade base oil

상압 잔사유 감압증류 공정, 감압 가스유 수소화 처리반응 공정, 감압 가스유 수소화분해반응 공정 및 분별증류 공정으로 이루어지는 수소화분해 공정에서, 분별증류 공정의 증류탑의 저부에서 배출되는 미전환유(UCO)를 상압잔사유 감압증류 공정으로 리사이클시켰다. 이때 상기 미전환유의 일부 또는 전부를 탑저 온도기준 300 내지 350℃의 온도 및 50 내지 300mmHg의 탑저 압력으로 운전되는, 별도의 미전환유 감압증류 공정으로 보내서 증류하고, 상기 미전환유 감압증류 공정에서 배출된 미전환유중 하기의 점도등급의 미전환유는 수소화 탈왁스 및 안정화 공정으로 진행시켜서, 점도가 100℃에서 3 내지 8 센티스톡이고, 점도지수가 100 이상인 고급 윤활기유를 제조하였다. 그리고 나머지 미전환유는 감압가스유 수소화 분해반응 공정으로 리사이클시켰다.The unconverted oil (UCO) discharged from the bottom of the distillation column in the fractionation distillation column is subjected to the atmospheric pressure in the hydrocracking process including the vacuum residue distillation process under reduced pressure, hydrogas treatment under reduced pressure gasification, hydrocracking under reduced pressure gas fractionation and fractionation distillation. The residue was recycled in a vacuum distillation process. At this time, a part or all of the unconverted oil is sent to a separate unconverted oil depressurization distillation process operated at a bottom temperature of 300 to 350 ° C. and a bottom pressure of 50 to 300 mmHg, and distilled, and discharged from the unconverted oil depressurization distillation process. The unconverted oil having the following viscosity grade in the unconverted oil was subjected to a hydrodewaxing and stabilization process to prepare a high grade lubricant base oil having a viscosity of 3 to 8 centistokes at 100 ° C. and a viscosity index of 100 or more. The remaining unconverted oil was recycled to a vacuum gas oil hydrocracking process.

그리하여 하기 표 1에서 보는 바와 같은 고급 윤활기유를 얻었다.Thus, an advanced lubricant base oil as shown in Table 1 below was obtained.

미전환유를 이용하여 제조된 고급 윤활기유의 성상Properties of Advanced Lubricant Base Oils Prepared with Unconverted Oil 기 유 3Base oil 3 기 유 4Base oil 4 기 유 6Base oil 6 점도 @ 40 ℃점도 @ 100 ℃Viscosity @ 40 ℃ Viscosity @ 100 ℃ 12.083.0112.083.01 18.554.0118.554.01 34.326.0534.326.05 점도지수Viscosity index 103103 114114 123123 아닐린점, ℃Aniline point, ℃ 104104 112112 121121 유동점, ℃Pour point, ℃ -27-27 -18-18 -12-12 방향족성분, wt%Aromatic component, wt% 0.20.2 1.51.5 0.30.3 나프텐성분, wt%Naphthenic component, wt% 62.462.4 63.763.7 71.071.0 파라핀성분, wt%Paraffin component, wt% 37.437.4 36.136.1 28.728.7

〈실험예〉 고급 윤활기유를 포함하는 동력식 조향장치 작동유 및 그의 성능시험<Experimental Example> Power Steering System Operating Oil Containing High Grade Lubricant Oil

실시예 1에서 제조된 고급 윤활기유 3 또는 4를 포함하는 동력식 조향장치 작동유를 하기의 시험방법을 통하여 타종의 기유를 포함하는 동력식 조향장치 작동유와 비교하여 마찰특성을 평가하였고, 그 결과를 다음 표 3에 나타내었다.Friction characteristics were evaluated by comparing the power steering hydraulic fluid including the high quality lubricant base oils 3 or 4 prepared in Example 1 with the power steering hydraulic fluid containing other base oils through the following test method. It is shown in Table 3 below.

시험기명 : SRV TesterTester Name: SRV Tester

마찰재 : 강제 디스크와 폴리테트라플루오로에틸렌제 블록Friction material: steel disk and block made of polytetrafluoroethylene

시험조건 : 진 폭 - 1.0 mmTest condition: true width-1.0 mm

진동수 - 50 HzFrequency-50 Hz

하 중 - 40 NLoad-40 N

하기 표 3의 비교예에서 사용한 타종의 기유는 하기 표 2과 같다.The base oil of the other species used in the comparative example of the following Table 3 is as Table 2 below.

비교예에 사용된 타종의 기유의 성상Properties of Other Oils Used in Comparative Examples 용제 추출Solvent extraction 수첨 개질Hydrogenation reforming 폴리알파올레핀Polyalphaolefin 점도 @ 40℃점도 @ 100℃Viscosity @ 40 ℃ Viscosity @ 100 ℃ 20.134.0920.134.09 20.174.1420.174.14 17.103.9117.103.91 점도지수Viscosity index 102102 106106 127127 아닐린점, ℃Aniline point, ℃ 101101 109109 125125 유동점, ℃Pour point, ℃ -15-15 -15-15 -54-54 방향족성분, wt%Aromatic component, wt% 29.729.7 4.54.5 0.00.0

본 발명의 고급 윤활기유를 포함하는 동력식 조향장치 작동유의 성능Performance of Motorized Steering System Hydraulic Oil Containing Advanced Lubricant Oil of the Invention 실시예 2Example 2 실시예 3Example 3 비교예 1Comparative Example 1 비교예 2Comparative Example 2 비교예 3Comparative Example 3 고급윤활기유 4Advanced Lubricant Oil 4 87.087.0 -- -- -- -- 고급 윤활기유 3Advanced Lubricants 3 -- 52.252.2 -- -- -- 용제추출기유Solvent Extraction Oil -- 34.834.8 87.087.0 -- -- 수첨매질기유Hydrogenated Medium Oil -- -- -- 87.087.0 -- 폴리알파올레핀Polyalphaolefin -- -- -- -- 87.087.0 첨가제 농축물Additive concentrate 6.06.0 6.06.0 6.06.0 6.06.0 6.06.0 점도지수 향상제Viscosity Index Improver 7.07.0 7.07.0 7.07.0 7.07.0 7.07.0 점도 @ 40℃Viscosity @ 40 ℃ 37.3737.37 35.6535.65 46.4446.44 43.3743.37 38.4838.48 점도 @ 100℃Viscosity @ 100 ℃ 7.837.83 7.677.67 8.748.74 8.588.58 7.527.52 점도지수Viscosity index 187187 192192 170170 180180 203203 아닐린점, ℃Aniline point, ℃ 109109 105105 9797 100100 114114 유동점, ℃Pour point, ℃ 〈 -50〈-50 〈 -50〈-50 -47.5-47.5 -47.5-47.5 〈 -50〈-50 저온브룩필드점도 @ -40℃, cPCold Brookfield Viscosity @ -40 ℃, cP 13,50013,500 15,50015,500 37,40037,400 33,10033,100 4,6004,600 고무침적시험(120℃, 72 hr)Rubber deposition test (120 ℃, 72 hr) PassPass PassPass PassPass PassPass FailFail SVR 마찰시험SVR Friction Test 0.0540.054 0.0570.057 0.0650.065 0.0620.062 0.0520.052

상기 실시예 2와 비교예 1,2 및 3을 보면, 실시예 1과 비교예 3의 경우가 저온점도특성, SRV 마찰시험에서 우수한 성능을 나타내고 있는 것을 표 3을 통하여 알 수 있다. 그러나 비교예 3의 경우 고무침적시험에서 성능상에 문제점이 있는 것으로 나타났다. 동력식 조향장치는 다양한 재질 및 형태의 고무가 밀봉을 위해 이용되므로 고무재와의 적합성은 중요한 성능 항목중의 하나이다.Looking at Example 2 and Comparative Examples 1,2 and 3, it can be seen from Table 3 that Example 1 and Comparative Example 3 exhibited excellent performance in low temperature viscosity characteristics and SRV friction test. However, in Comparative Example 3, there was a problem in performance in the rubber deposition test. Since the power steering system uses rubber of various materials and types for sealing, compatibility with rubber materials is one of the important performance items.

실시예 3과 비교예 1을 비교하여 보면, 미전환유를 이용한 고급 윤활기유를 일부 적용한 실시예 3은 용제추출기유만을 사용한 비교예 1보다 우수한 저온특성 및 마찰 특성을 가지고 있는 것으로 나타났다.Comparing Example 3 and Comparative Example 1, it was shown that Example 3 to which some of the high-grade lubricant base oil using unconverted oil has better low temperature characteristics and friction characteristics than Comparative Example 1 using only solvent extraction base oil.

이상에서 보는 바와 같이 본 발명의 고급 윤활기유를 함유하는 동력식 조향장치 작동유은 마찰계수가 낮으므로 타종의 기유를 사용하는 경우와 비교할 때 조향장치내 각종 습동부에서 발생할 수 있는 소음을 효과적으로 감소시킬 수 있다. 따라서 본 발명의 동력식 조향장치 작동류 조성물을 동력식 조향장치에 사용하게 되면 소음이 적은, 즉 정숙성을 유지할 수 있는 동력식 조향장치를 실현할 수 있게 된다.As described above, the power steering system hydraulic fluid containing the high-grade lubricating base oil of the present invention has a low coefficient of friction, which can effectively reduce the noise that may occur in various sliding parts in the steering system as compared with the case of using other types of base oils. have. Therefore, when the power steering apparatus hydraulic flow composition of the present invention is used in the power steering apparatus, it is possible to realize a power steering apparatus with low noise, that is, maintaining quietness.

Claims (6)

상압 잔사유 감압증류 공정, 감압 가스유 수소화 처리반응 공정, 감압 가스유 수소화분해반응 공정 및 분별증류 공정으로 구성된 수소화 분해공정에서 미전환유(UCO)를 상기 분별증류 공정으로부터 상기 감압 가스유 수소화분해 공정으로 리사이클시키는 리사이클 모드의 연료유 수소화 분해 공정에 있어서, 상기 미전환유의 일부 또는 전부를 별도의 미전환유 감압증류 공정으로 보내서 분리하여 제조되는, 점도가 100℃에서 3 내지 8 센티스톡이고, 점도지수가 100 이상인 고급 윤활기유를 포함하는 동력식 조향장치의 작동유.In the hydrocracking process consisting of an atmospheric residue oil distillation under reduced pressure distillation, a vacuum gas oil hydrotreating process, a vacuum gas oil hydrocracking process, and a fractional distillation process, unconverted oil (UCO) is removed from the fractional distillation process. In the fuel oil hydrocracking process of the recycle mode for recycling in a recycle mode, a part or all of the unconverted oil is separated and sent to a separate unconverted oil vacuum distillation process, and has a viscosity of 3 to 8 centistokes at 100 ° C., and a viscosity index. Hydraulic oil of the power steering system containing a high grade lubricant base oil of 100 or more. 제1항에 있어서, 미전환유 감압공정이 탑저 온도기준으로 300 내지 350℃의 온도 및 탑저 압력기준으로 50 내지 300mmHg의 압력으로 운전되는 것을 특징으로 하는, 고급 윤활기유를 포함하는 동력식 조향장치의 작동유.The method of claim 1, wherein the non-converted oil decompression process is operated at a temperature of 300 to 350 ℃ on the basis of the bottom temperature and a pressure of 50 to 300mmHg on the basis of the bottom pressure, Working oil. 제1항에 있어서, 미전환유 감압공정이 수소화 탈왁스 및 안정화 공정을 포함하는 것을 특징으로 하는, 고급 윤활기유를 포함하는 동력식 조향장치의 작동유.2. The hydraulic oil of a powered steering apparatus according to claim 1, wherein the unconverted oil depressurization process includes a hydrodeswaxing and stabilization process. 제1항에 있어서, 고급 윤활기유가 나프텐 성분 55 내지 75중량%, 파라핀 성분 40 내지 25중량% 및 방향족 성분 0 내지 5중량%로 구성되는 것을 특징으로 하는, 고급 윤활기유를 포함하는 동력식 조향장치의 작동유.2. Powered steering according to claim 1, characterized in that the higher lubricating base oil comprises 55 to 75% by weight naphthenic component, 40 to 25% by weight paraffin component and 0 to 5% by weight aromatic component. Working oil of the device. 제1항 또는 제4항에 있어서, 미전환유 감압증류 공정에 의해 산출되는 고급 윤활기유와 타종의 기유를 포함하며, 이때 상기 고급 윤활기유를 10중량% 이상 포함하는 것을 특징으로 하는 동력식 조향장치의 작동유.5. The motorized steering apparatus according to claim 1 or 4, comprising high grade lubricating base oil and other kinds of base oils calculated by the unconverted oil depressurization distillation process, wherein the high grade lubricating base oil comprises at least 10% by weight. Working oil. 제5항에 있어서, 상기 고급 윤활기유가 50 내지 80중량%임을 특징으로 하는 동력식 조향장치의 작동유.6. The hydraulic oil of a powered steering device according to claim 5, wherein the high quality lubricant base oil is 50 to 80% by weight.
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KR100831813B1 (en) 2007-04-11 2008-05-28 에스케이에너지 주식회사 The method of preparing naphthenic lube base oil from aromatic extract and the naphthenic base oil using the method

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KR101679426B1 (en) * 2010-04-30 2016-11-25 에스케이이노베이션 주식회사 A method of preparing high graded lube base oil using unconverted oil

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KR100831813B1 (en) 2007-04-11 2008-05-28 에스케이에너지 주식회사 The method of preparing naphthenic lube base oil from aromatic extract and the naphthenic base oil using the method

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