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公开(公告)号：KR101683512B1
公开(公告)日：2016-12-07
申请号：KR1020150044461
申请日：2015-03-30
Applicant: 현대자동차주식회사 , 훼브 유럽 게엠베하
CPC classification number: F01N3/0814 , F01N3/035 , F01N3/0835 , F01N3/0842 , F01N3/2066 , F01N3/2073 , F01N3/208 , F01N9/005 , F01N13/009 , F01N2250/12 , F01N2430/06 , F01N2560/025 , F01N2560/026 , F01N2560/06 , F01N2570/12 , F01N2570/14 , F01N2570/18 , F01N2610/02 , F01N2610/146 , F01N2900/0412 , F01N2900/0418 , F01N2900/0601 , F01N2900/1402 , F01N2900/1602 , F01N2900/1614 , F01N2900/1616 , F01N2900/1618 , F02D41/0275 , F02D2041/1433 , F02D2200/0806 , Y02T10/24 , Y02T10/47
Abstract: 본발명의실시예에따른린 녹스트랩(Lean Nox Trap; LNT)의재생시 환원되는질소산화물의양을계산하는방법은배기가스정화장치의 LNT에유입되는 C3H6의질량유량중 NOx 환원에사용되는 C3H6의질량유량을계산하는단계; LNT에유입되는 NH3의질량유량중 NOx 환원에사용되는 NH3의질량유량을계산하는단계; 상기 NOx 환원에사용되는 C3H6의질량유량과 NH3의질량유량을기초로환원된 NOx 질량유량을계산하는단계; 그리고상기환원된 NOx 질량유량을재생기간동안적분하여환원된 NOx량을계산하는단계;를포함할수 있다.
Abstract translation: 林根据本发明实施例的熔化带。计算的氮氧化物的量的方法（稀燃NOx捕集LNT）被用于NO x还原的C3H6的质量流率在一个排气净化装置进入LNT的再现期间被减少 计算C3H6的质量流率; 计算流入LNT的NH3的质量流率中用于NOx还原的NH3的质量流率; 基于C3H6的质量流率和用于NOx还原的NH3的质量流量计算减少的NOx质量流量; 并且在再生期间积分减少的NOx质量流量以计算减少的NOx量。
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公开(公告)号：KR1020160116572A
公开(公告)日：2016-10-10
申请号：KR1020150044461
申请日：2015-03-30
Applicant: 현대자동차주식회사 , 훼브 유럽 게엠베하
CPC classification number: F01N3/0814 , F01N3/035 , F01N3/0835 , F01N3/0842 , F01N3/2066 , F01N3/2073 , F01N3/208 , F01N9/005 , F01N13/009 , F01N2250/12 , F01N2430/06 , F01N2560/025 , F01N2560/026 , F01N2560/06 , F01N2570/12 , F01N2570/14 , F01N2570/18 , F01N2610/02 , F01N2610/146 , F01N2900/0412 , F01N2900/0418 , F01N2900/0601 , F01N2900/1402 , F01N2900/1602 , F01N2900/1614 , F01N2900/1616 , F01N2900/1618 , F02D41/0275 , F02D2041/1433 , F02D2200/0806 , Y02T10/24 , Y02T10/47
Abstract: 본발명의실시예에따른린 녹스트랩(Lean Nox Trap; LNT)의재생시 환원되는질소산화물의양을계산하는방법은배기가스정화장치의 LNT에유입되는 C3H6의질량유량중 NOx 환원에사용되는 C3H6의질량유량을계산하는단계; LNT에유입되는 NH3의질량유량중 NOx 환원에사용되는 NH3의질량유량을계산하는단계; 상기 NOx 환원에사용되는 C3H6의질량유량과 NH3의질량유량을기초로환원된 NOx 질량유량을계산하는단계; 그리고상기환원된 NOx 질량유량을재생기간동안적분하여환원된 NOx량을계산하는단계;를포함할수 있다.
Abstract translation: 计算在再生期间从贫NOx捕集器（LNT）减少的氮氧化物（NOx）质量的方法包括计算用于减少流入排气净化装置的LNT的C3H6质量流中的NOx的C3H6质量流，计算 用于减少在LNT中产生的NH 3质量流中的NO x的NH 3质量流量，基于用于减少NOx和用于减少NOx的NH 3质量流量的C3H6质量流量计算降低的NOx质量流量，并计算减少的 通过在再生时段内整合减少的NOx质量流量的NOx质量。
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公开(公告)号：KR1020150078190A
公开(公告)日：2015-07-08
申请号：KR1020130167364
申请日：2013-12-30
Applicant: 현대자동차주식회사
Inventor： 박진우
IPC: C22C38/02
CPC classification number: C22C38/02
Abstract: 본발명은우수한인성, 피로수명및 내부식성등을요구하는스프링등에이용되는조성물에관한것으로, 보다상세하게는전체조성물중량에대하여탄소(C) 0.5~0.55중량%, 실리콘(Si) 1.4~1.7중량%, 니켈(Ni) 0.3~0.5중량%, 나이오븀(Nb) 0.01~0.04중량%, 구리(Cu) 0.25~0.35중량%, 붕소(B) 0.0005~0.0025중량% 및잔부의철(Fe)과불가피한불순물등을포함함으로써, 미세조직사이의결합력을증가시켜강도등을향상시키고, 나이오븀(Nb) 등으로미세조직을더욱미세화하여인성등을향상시킬수 있으며, 일반피로수명, 부식피로수명및 내부식성등을더욱향상시킬수 있는내구성이향상된코일스프링조성물에관한것이다.
Abstract translation: 本发明涉及一种用于需要优异的韧性，耐疲劳寿命和耐腐蚀性的弹簧的组合物。 更具体地说，本发明涉及具有改善的耐久性的螺旋弹簧组合物，该组合物由0.5-0.55重量％的C，1.4-1.7重量％的Si，0.3-0.5重量％的Ni，0.01-0.04重量％的 Nb，0.25-0.35重量％的Cu，0.0005-0.0025重量％的B，余量的Fe和基于组合物的总重量的杂质。 因此，螺旋弹簧组合物随着微观结构之间的结合力的增加而提高强度; 通过使Nb等微细化而提高韧性; 并提高一般疲劳寿命，腐蚀疲劳寿命和耐腐蚀性。
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公开(公告)号：KR101534699B1
公开(公告)日：2015-07-07
申请号：KR1020130161436
申请日：2013-12-23
Applicant: 현대자동차주식회사
Inventor： 박진우
CPC classification number: Y02T10/47
Abstract: 본발명은질소산화물저감촉매의탈황이필요한경우질소산화물저감촉매의탈황을진행할수 잇는추천경로를제공함으로써질소산화물저감촉매의성능저하를방지하는질소산화물저감촉매의탈황장치및 탈황방법에관한것이다. 상기질소산화물저감촉매의탈황방법은내비게이션장치로경로를탐색하는지판단하는단계; 경로를탐색하면질소산화물저감촉매의탈황이필요한지를판단하는단계; 질소산화물저감촉매의탈황이필요하면, 질소산화물저감촉매의탈황이가능한경로를추천하는단계; 추천된경로로주행하는지를판단하는단계; 추천된경로로주행중이면질소산화물저감촉매의탈황조건을만족하는지판단하는단계; 그리고질소산화물저감촉매의탈황조건을만족하면, 질소산화물저감촉매의탈황을진행하는단계;를포함할수 있다.
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公开(公告)号：KR1020150073576A
公开(公告)日：2015-07-01
申请号：KR1020130161436
申请日：2013-12-23
Applicant: 현대자동차주식회사
Inventor： 박진우
Abstract: 본발명은질소산화물저감촉매의탈황이필요한경우질소산화물저감촉매의탈황을진행할수 잇는추천경로를제공함으로써질소산화물저감촉매의성능저하를방지하는질소산화물저감촉매의탈황장치및 탈황방법에관한것이다. 상기질소산화물저감촉매의탈황방법은내비게이션장치로경로를탐색하는지판단하는단계; 경로를탐색하면질소산화물저감촉매의탈황이필요한지를판단하는단계; 질소산화물저감촉매의탈황이필요하면, 질소산화물저감촉매의탈황이가능한경로를추천하는단계; 추천된경로로주행하는지를판단하는단계; 추천된경로로주행중이면질소산화물저감촉매의탈황조건을만족하는지판단하는단계; 그리고질소산화물저감촉매의탈황조건을만족하면, 질소산화물저감촉매의탈황을진행하는단계;를포함할수 있다.
Abstract translation: 本发明涉及一种氮氧化物还原催化剂的脱硫装置，其能够通过提供氮氧化物还原催化剂脱硫的推荐路径来防止氮氧化物还原催化剂的性能降解，如果需要氮氧化物还原催化剂的脱硫; 和脱硫方法。 氮氧化物还原催化剂的脱硫方法包括：确定导航装置是否搜索路径的步骤; 如果搜索路径，则确定氮氧化物还原催化剂是否需要脱硫的步骤; 如果需要氮氧化物还原催化剂的脱硫，则推荐氮氧化物还原催化剂的脱硫路径的步骤; 确定是否在推荐路径上行驶的步骤; 确定在推荐路径上行驶时是否满足氮氧化物还原催化剂的脱硫条件的步骤; 如果满足氮氧化物还原催化剂的脱硫条件，则进行氮氧化物还原催化剂的脱硫的工序。
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Patent Agency Ranking
公开(公告)号：KR1020130017957A
公开(公告)日：2013-02-20
申请号：KR1020110080718
申请日：2011-08-12
Applicant: 현대자동차주식회사
CPC classification number: F02D41/028 , F02D41/029 , F02D2200/0812
Abstract: PURPOSE: A desulfurization method of a nitrogen oxide absorbing catalyst system is provided to simplify the regeneration logic of desulfurization by deciding the desulfurization time based on the number of success in the regeneration of DPF(Diesel Particulate Filter), since all the trace sulfur compounds included in the exhaust gas ejected when the ultra low sulfur diesel oil is used become poison to an LNT(Lean NOx Trap) catalyst. CONSTITUTION: A desulfurization method of a nitrogen oxide absorbing catalyst system comprises the following steps: determining(S110) whether the number of the success of DPF regeneration reaches the predetermined number of the success of DPF regeneration or not; performing(S120) desulfurization by terminating the DPF regeneration when the number of success of the DPF regeneration reaches the predetermined number of success of the DPF regeneration; entering the desulfurization mode; terminating(S160) the desulfurization after performing the desulfurization for the predetermined time; calculating and calibrating(S170) the amount of the collected PM-10(fine dust) in the DPF generated during the time of desulfurization after the termination of the desulfurization; determining the time for the following DPF regeneration; and comparing the temperature(T) of the inside of the nitrogen oxide absorbing catalyst with the deterioration temperature(X) of the nitrogen oxide absorbing catalyst during the time of the desulfurization. [Reference numerals] (S100) Normal NO_X purification operation mode; (S110) Reaching a predetermined number of success of DPF regeneration?; (S120) Immediately entering a desulfurization mode after terminating the DPF regeneration; (S130) Maintaining a lambda(λ) value below a predetermined value; (S140) LNT catalyst inside temperature(T) > Deterioration temperature(X) ?; (S150) Desulfurization for a predetermined time?; (S160) Terminating the desulfurization; (S170) Calculating and correcting the amount of PM collected in a DPF caused by PM produced during the desulfurization; (S180) Switching the mode to a normal lean operation for preventing overheating of catalyst; (S190) LNT catalyst inside temperature(T) ≤ Predetermined temperature(Y)
Abstract translation: 目的：提供一种氮氧化物吸收催化剂体系的脱硫方法，以便通过根据DPF（柴油颗粒过滤器）再生成功次数决定脱硫时间，从而简化脱硫再生逻辑，因为所有痕量硫化合物均包括 当使用超低硫柴油时排出的废气对LNT（Lean NOx Trap）催化剂变毒。 构成：氮氧化物吸收催化剂体系的脱硫方法包括以下步骤：确定（S110）DPF再生的成功次数是否达到DPF再生的成功的预定数量; 当DPF再生的成功次数达到预定次数的DPF再生时，通过终止DPF再生来执行（S120）脱硫; 进入脱硫模式; 在规定时间内终止（S160）脱硫后的脱硫; 计算和校准（S170）脱硫结束后脱硫时产生的DPF中收集的PM-10（细粉尘）的量; 确定以下DPF再生的时间; 并将氮氧化物吸收催化剂的内部的温度（T）与脱硫时的氮氧化物吸收催化剂的劣化温度（X）进行比较。 （附图标记）（S100）正常NO_X净化操作模式; （S110）达到预定数量的DPF再生成功; （S120）终止DPF再生后立即进入脱硫模式; （S130）维持低于预定值的λ（λ）值; （S140）LNT催化剂内部温度（T）>劣化温度（X） （S150）脱硫预定时间？ （S160）终止脱硫; （S170）计算和校正在脱硫期间由PM产生的DPF中收集的PM的量; （S180）将模式切换为正常的稀薄操作，以防止催化剂过热; （S190）LNT催化剂内部温度（T）≤预定温度（Y）
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公开(公告)号：KR1020120000419A
公开(公告)日：2012-01-02
申请号：KR1020100060771
申请日：2010-06-25
Applicant: 현대자동차주식회사
Inventor： 박진우
Abstract: PURPOSE: A steel for a cage of a constant velocity joint and a cage of a constant velocity joint using the same are provided to improve intensity and impact toughness of a cage capering to the existing material cage. CONSTITUTION: A steel for a cage of a constant velocity joint comprises carbon(C) of less than 0.12~0.18 weight%, silicon(Si) of 0.10~0.20 weight%, manganese(Mn) of 1.20~1.50 weight%, phosphorus(P) of less than 0.03 weight%, nickel(Ni) of 0.50~1.00 weight%, sulfur(S) of less than 0.03 weight%, chrome(Cr) of 0.20~0.40 weight%, titanium(Ti) of 0.02~0.05 weight%, nitrogen(N) of 0.01~0.02 weight%, aluminum(Al) of 0.01~0.03 weight%, boron(B) of 10~40ppm, and iron remainder(Fe). A cage(15) of constant velocity joint is located between an inner-race(13) and an outer-race(12). The iron is the main component of the cage. The cage of the constant velocity joint regulates the location of the axial direction and radial direction of the inner-race and outer-race.
Abstract translation: 目的：提供一种用于恒速接头保持架的钢和使用其的等速万向节保持架，以提高对现有材料保持架的笼式铆钉的强度和冲击韧性。 构成：用于恒速接头保持架的钢包括小于0.12〜0.18重量％的碳（C），0.10〜0.20重量％的硅（Si），1.20〜1.50重量％的锰（Mn），磷（ P）小于0.03重量％，镍（Ni）为0.50〜1.00重量％，硫（S）小于0.03重量％，铬（Cr）为0.20〜0.40重量％，钛（Ti）为0.02〜0.05 重量％，氮（N）0.01〜0.02重量％，铝（Al）0.01〜0.03重量％，硼（B）10〜40ppm，铁余量（Fe）。 恒速接头的保持架（15）位于内圈（13）和外圈（12）之间。 铁是笼子的主要部件。 等速万向节的笼子调节内圈和外圈的轴向和径向的位置。
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公开(公告)号：KR1020110062617A
公开(公告)日：2011-06-10
申请号：KR1020090119396
申请日：2009-12-03
Applicant: 현대자동차주식회사
CPC classification number: Y02A50/2322 , Y02T10/47 , F01N3/20 , F01N3/28 , F01N2560/025 , F01N2610/146
Abstract: PURPOSE: A device and method for purifying secondary injection exhaust gas from vehicle is provided to improve the purifying efficiency of exhaust gas following with the dynamic operation of an engine. CONSTITUTION: A device and method for purifying secondary injection exhaust gas from vehicle comprises a harmful material purification catalyst(10), a secondary injection system, and a controller(40). The harmful material purification catalyst is installed in the fixed position of an exhaust pipe(6) connected to an engine(2). The secondary injection system supplies reducing agent or fuel to catalyst. The controller determines an operation section according to engine RPM and fuel ejection amount under a secondary spray condition. The controller determines a secondary fuel injection pattern by applying a secondary ejection map based on the operation section. The controller purifies NOx and particulate matters by supplying fuel or reducing agent to catalyst using the secondary injection system.
Abstract translation: 目的：提供一种用于净化车辆二次注入废气的装置和方法，以提高发动机动态运行后废气的净化效率。 构成：用于净化车辆二次注入废气的装置和方法包括有害物质净化催化剂（10），二次注射系统和控制器（40）。 有害物质净化催化剂安装在与发动机（2）连接的排气管（6）的固定位置。 二次注射系统向催化剂供应还原剂或燃料。 控制器根据发动机RPM和二次喷射状态下的燃料喷射量确定操作部。 控制器通过基于操作部分应用二次喷射图来确定二次燃料喷射模式。 控制器通过使用二次注射系统向催化剂供应燃料或还原剂来净化NOx和颗粒物质。
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公开(公告)号：KR1020100064069A
公开(公告)日：2010-06-14
申请号：KR1020080122496
申请日：2008-12-04
Applicant: 현대자동차주식회사
Inventor： 박진우
CPC classification number: Y02T10/40 , F01M11/10 , F01M1/20 , F01M2011/1446 , F02D41/222 , F02D2041/228
Abstract: PURPOSE: An oil pressure monitoring method for a diesel engine is provided to enable a user to check the time to replace engine oil by determining the oil replacement of a diesel engine through the oil pressure of a diesel engine. CONSTITUTION: An oil pressure monitoring method for a diesel engine comprises following steps. Whether a vehicle has moved over constant mileage or a vehicle is traveled up to constant km after the completion of post-injection is determined(S16). If the first step is satisfied, whether or not an engine operation condition for measuring engine oil pressure is measured is determined(S18). If the second step is satisfied, whether or not the operation condition of the second step is maintained for fixed time(S20). If the third step is satisfied, the engine oil pressure is measured(S22). Whether or not the engine oil pressure measured in the fourth step is less than the preset limit value at the engine drive condition of the second step(S24).
Abstract translation: 目的：提供一种用于柴油发动机的油压监测方法，用于通过柴油发动机的油压确定柴油机的换油来检查更换机油的时间。 构成：柴油机的油压监测方法包括以下步骤。 确定后喷射完成后车辆是否已经超过恒定里程或车辆行驶到恒定公里（S16）。 如果满足第一步骤，则确定是否测量发动机油压的发动机运转条件（S18）。 如果第二步满足，则第二步的操作条件是否保持固定时间（S20）。 如果满足第三步，则测量发动机油压（S22）。 在第四步骤中测量的发动机机油压力是否小于第二步骤的发动机驱动条件下的预设极限值（S24）。
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公开(公告)号：KR100962812B1
公开(公告)日：2010-06-09
申请号：KR1020070131477
申请日：2007-12-14
Applicant: 현대자동차주식회사
Inventor： 박진우
CPC classification number: Y02T10/47
Abstract: 본 발명은 디젤엔진 배기가스 저감 장치에 관한 것으로, 일측에 산소 분사 신호에 따라 압축되어 있던 산소를 분사하는 산소압축/분사부; 및 배기가스의 산소량을 감지하여 상기 산소량이 소정의 기준 산소량 미만인 경우에 상기 산소압축/분사부로 상기 산소 분사 신호를 인가하는 산소 감지부를 포함함으로써, CPF 전단의 산소량을 일정 수준 이상으로 유지할 수 있어 LNT 탈황과 CPF 재생의 연비를 개선시킬 수 있다.
배기가스, CPF, LNT
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