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1. 发明授权

US08123931B2 Catalyst for hydrocarbon steam cracking, method of preparing the same and method of preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的催化剂，其制备方法和使用该催化剂制备烯烃的方法
公开(公告)号：US08123931B2
公开(公告)日：2012-02-28
申请号：US12154656
申请日：2008-05-23
申请人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： C10G11/04
CPC分类号： B01J23/26 , B01J21/063 , B01J21/066 , B01J23/002 , B01J35/0033 , B01J37/0009 , B01J37/031 , B01J2523/00 , C07C4/06 , C07C2521/06 , C07C2523/26 , C10G11/02 , C10G11/05 , C10G11/10 , C10G11/16 , C10G11/18 , C10G11/20 , C10G2300/4018 , C10G2400/20 , C07C11/02 , B01J2523/47 , B01J2523/48 , B01J2523/67
摘要： The present invention relates to a catalyst for hydrocarbon steam cracking for the production of light olefin, a preparation method of the catalyst and a preparation method of olefin by using the same. More precisely, the present invention relates to a composite catalyst prepared by mixing the oxide catalyst powder represented by CrZrjAkOx (0.5≦j≦120, 0≦k≦50, A is a transition metal, x is the number satisfying the condition according to valences of Cr, Zr and A, and values of j and k) and carrier powder and sintering thereof, a composite catalyst wherein the oxide catalyst is impregnated on a carrier, and a method of preparing light olefin such as ethylene and propylene by hydrocarbon steam cracking in the presence of the composite catalyst. The composite catalyst of the present invention has excellent thermal/mechanical stability in the cracking process, and has less inactivation rate by coke and significantly increases light olefin yield.
摘要翻译：本发明涉及一种用于生产轻质烯烃的烃蒸汽裂化催化剂，该催化剂的制备方法和使用它的烯烃的制备方法。更确切地说，本发明涉及通过混合由CrZrjAkOx（0.5＆amp; NlE; j＆nlE; 120,0＆amp; NlE; k＆nlE; 50表示的氧化物催化剂粉末）制备的复合催化剂，A是过渡金属，x是满足根据 Cr，Zr和A的价数，以及j和k的值以及载体粉末及其烧结，其中氧化物催化剂浸渍在载体上的复合催化剂，以及通过烃蒸汽制备轻质烯烃如乙烯和丙烯的方法在复合催化剂存在下开裂。本发明的复合催化剂在裂化过程中具有优异的热/机械稳定性，并且焦炭的失活率较低，并显着提高轻烯烃产率。

2. 发明申请

US20090105066A1 Catalyst for hydrocarbon steam cracking, method of preparing the same and method of preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的催化剂，其制备方法和使用该催化剂制备烯烃的方法
公开(公告)号：US20090105066A1
公开(公告)日：2009-04-23
申请号：US12154656
申请日：2008-05-23
申请人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： B01J21/00 , B01J23/26 , B01J21/08 , B01J29/06 , B01J27/224
CPC分类号： B01J23/26 , B01J21/063 , B01J21/066 , B01J23/002 , B01J35/0033 , B01J37/0009 , B01J37/031 , B01J2523/00 , C07C4/06 , C07C2521/06 , C07C2523/26 , C10G11/02 , C10G11/05 , C10G11/10 , C10G11/16 , C10G11/18 , C10G11/20 , C10G2300/4018 , C10G2400/20 , C07C11/02 , B01J2523/47 , B01J2523/48 , B01J2523/67
摘要： The present invention relates to a catalyst for hydrocarbon steam cracking for the production of light olefin, a preparation method of the catalyst and a preparation method of olefin by using the same. More precisely, the present invention relates to a composite catalyst prepared by mixing the oxide catalyst powder represented by CrZrjAkOx (0.5≦j≦120, 0≦k≦50, A is a transition metal, x is the number satisfying the condition according to valences of Cr, Zr and A, and values of j and k) and carrier powder and sintering thereof, a composite catalyst wherein the oxide catalyst is impregnated on a carrier, and a method of preparing light olefin such as ethylene and propylene by hydrocarbon steam cracking in the presence of the composite catalyst. The composite catalyst of the present invention has excellent thermal/mechanical stability in the cracking process, and has less inactivation rate by coke and significantly increases light olefin yield.
摘要翻译：本发明涉及一种用于生产轻质烯烃的烃蒸汽裂化催化剂，该催化剂的制备方法和使用它的烯烃的制备方法。更准确地说，本发明涉及通过混合由CrZrjAkOx（0.5≤j≤1,0,0≤k≤50）表示的氧化物催化剂粉末制备的复合催化剂，A是过渡金属，x是满足根据Cr，Zr和A的化合价，以及j和k值和载体粉末的条件和其烧结，其中氧化物催化剂浸渍在载体上的复合催化剂，以及制备轻质烯烃如乙烯和丙烯的方法在复合催化剂存在下通过烃蒸汽裂化。本发明的复合催化剂在裂化过程中具有优异的热/机械稳定性，并且焦炭的失活率较低，并显着提高轻烯烃产率。

3. 发明授权

US08492305B2 Catalyst for hydrocarbon steam cracking, method of preparing the same and method of preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的催化剂，其制备方法和使用该催化剂制备烯烃的方法
公开(公告)号：US08492305B2
公开(公告)日：2013-07-23
申请号：US13309257
申请日：2011-12-01
申请人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： B01J23/26
CPC分类号： B01J23/26 , B01J21/063 , B01J21/066 , B01J23/002 , B01J35/0033 , B01J37/0009 , B01J37/031 , B01J2523/00 , C07C4/06 , C07C2521/06 , C07C2523/26 , C10G11/02 , C10G11/05 , C10G11/10 , C10G11/16 , C10G11/18 , C10G11/20 , C10G2300/4018 , C10G2400/20 , C07C11/02 , B01J2523/47 , B01J2523/48 , B01J2523/67
摘要： The present invention relates to a catalyst for hydrocarbon steam cracking for the production of light olefin, a preparation method of the catalyst and a preparation method of olefin by using the same. More precisely, the present invention relates to a composite catalyst prepared by mixing the oxide catalyst powder represented by CrZrjAkOx (0.5≦j≦120, 0≦k≦50, A is a transition metal, x is the number satisfying the condition according to valences of Cr, Zr and A, and values of j and k) and carrier powder and sintering thereof, a composite catalyst wherein the oxide catalyst is impregnated on a carrier, and a method of preparing light olefin such as ethylene and propylene by hydrocarbon steam cracking in the presence of the composite catalyst. The composite catalyst of the present invention has excellent thermal/mechanical stability in the cracking process, and has less inactivation rate by coke and significantly increases light olefin yield.
摘要翻译：本发明涉及一种用于生产轻质烯烃的烃蒸汽裂化催化剂，该催化剂的制备方法和使用它的烯烃的制备方法。更确切地说，本发明涉及通过将CrZrjAkOx（0.5≤j≤120,0≤k≤50）表示的氧化物催化剂粉末混合而成的复合催化剂，A是过渡金属，x是满足根据化合价的条件的数的Cr，Zr和A，以及j和k的值和载体粉末及其烧结，其中氧化物催化剂浸渍在载体上的复合催化剂，以及通过烃蒸汽裂解制备轻质烯烃如乙烯和丙烯的方法在复合催化剂的存在下。本发明的复合催化剂在裂化过程中具有优异的热/机械稳定性，并且焦炭的失活率较低，并显着提高轻烯烃产率。

4. 发明授权

US08242047B2 Oxide catalyst and phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and method for preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其制备方法和使用该方法制备烯烃
公开(公告)号：US08242047B2
公开(公告)日：2012-08-14
申请号：US13072493
申请日：2011-03-25
申请人： Jun-seon Choi , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-seon Choi , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： B01J23/00 , C01G37/14 , C01G23/00 , C01G25/02
CPC分类号： B01J27/188 , B01J21/066 , B01J23/002 , B01J23/26 , B01J23/86 , B01J37/03 , B01J2523/00 , B01J2523/13 , B01J2523/22 , B01J2523/51 , C10G11/04 , C10G2300/4006 , C10G2300/4018 , C10G2300/70 , C10G2300/807 , C10G2400/20 , B01J2523/3712 , B01J2523/48 , B01J2523/67 , B01J2523/47
摘要： The present invention relates to an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and a method for preparing olefin by using the same. More precisely, the present invention relates to an oxide catalyst for hydrocarbon steam cracking represented by formula 1 and a phosphoric oxide catalyst for hydrocarbon steam cracking represented by formula 3 which would be used for the production of olefin such as ethylene and propylene by hydrocarbon steam cracking, and a method for preparing the same. The present invention provides an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking that has excellent thermo-stability at high temperature and improved olefin yield. CrZrjAkOx [Formula 1] CrZrjAkPlOx [Formula 3] Wherein, j, k, l and x are as indicated in the description.
摘要翻译：本发明涉及一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其制备方法和使用该方法制备烯烃的方法。更确切地说，本发明涉及由式1表示的烃蒸汽裂解用氧化物催化剂和由式3表示的烃蒸汽裂解用磷酸氧化物催化剂，其用于通过烃蒸汽裂解生产烯烃如乙烯和丙烯，及其制备方法。本发明提供了一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其在高温下具有优异的热稳定性和提高的烯烃产率。 CrZrjAkOx [式1] CrZrjAkP10x [式3]其中，j，k，l和x如说明书中所示。

5. 发明申请

US20080081008A1 Oxide catalyst and phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and method for preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其制备方法和使用该方法制备烯烃
公开(公告)号：US20080081008A1
公开(公告)日：2008-04-03
申请号：US11902665
申请日：2007-09-24
申请人： Jun-seon Choi , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-seon Choi , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： C01G37/02
CPC分类号： B01J27/188 , B01J21/066 , B01J23/002 , B01J23/26 , B01J23/86 , B01J37/03 , B01J2523/00 , B01J2523/13 , B01J2523/22 , B01J2523/51 , C10G11/04 , C10G2300/4006 , C10G2300/4018 , C10G2300/70 , C10G2300/807 , C10G2400/20 , B01J2523/3712 , B01J2523/48 , B01J2523/67 , B01J2523/47
摘要： The present invention relates to an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and a method for preparing olefin by using the same. More precisely, the present invention relates to an oxide catalyst for hydrocarbon steam cracking represented by formula 1 and a phosphoric oxide catalyst for hydrocarbon steam cracking represented by formula 3 which would be used for the production of olefin such as ethylene and propylene by hydrocarbon steam cracking, and a method for preparing the same. The present invention provides an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking that has excellent thermo-stability at high temperature and improved olefin yield. CrZrjAkOx [Formula 1] CrZrjAkPlOx [Formula 3]Wherein, j, k, l and x are as indicated in the description.
摘要翻译：本发明涉及一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其制备方法和使用该方法制备烯烃的方法。更确切地说，本发明涉及由式1表示的烃蒸汽裂解用氧化物催化剂和由式3表示的烃蒸汽裂解用磷酸氧化物催化剂，其用于通过烃蒸汽裂解生产烯烃如乙烯和丙烯，及其制备方法。本发明提供了一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其在高温下具有优异的热稳定性和提高的烯烃产率。 <？in-line-formula description =“In-line Formulas”end =“lead”？> CrZr 公式1] <？in-line-formula description =“In-line Formulas”end =“tail”？> <？in-line-formula description =“In-line Formulas”end =“lead”？> CrZr _{其中，j，k，l和x如说明书中所示。}

6. 发明授权

US08569200B2 Catalyst for hydrocarbon steam cracking, method of preparing the same and method of preparing olefin by using the same 有权
标题翻译：用于烃蒸汽裂化的催化剂，其制备方法和使用该催化剂制备烯烃的方法
公开(公告)号：US08569200B2
公开(公告)日：2013-10-29
申请号：US13309241
申请日：2011-12-01
申请人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： B01J21/06
CPC分类号： B01J23/26 , B01J21/063 , B01J21/066 , B01J23/002 , B01J35/0033 , B01J37/0009 , B01J37/031 , B01J2523/00 , C07C4/06 , C07C2521/06 , C07C2523/26 , C10G11/02 , C10G11/05 , C10G11/10 , C10G11/16 , C10G11/18 , C10G11/20 , C10G2300/4018 , C10G2400/20 , C07C11/02 , B01J2523/47 , B01J2523/48 , B01J2523/67
摘要： A catalyst for hydrocarbon steam cracking for the production of light olefin, a preparation method of the catalyst and a preparation method of olefin by using the same. More precisely, the present invention relates to a composite catalyst prepared by mixing the oxide catalyst powder represented by CrZrjAkOx (0.5≦j≦120, 0≦k≦50, A is a transition metal, x is the number satisfying the condition according to valences of Cr, Zr and A, and values of j and k) and carrier powder and sintering thereof, a composite catalyst wherein the oxide catalyst is impregnated on a carrier, and a method of preparing light olefin such as ethylene and propylene by hydrocarbon steam cracking in the presence of the composite catalyst. The composite catalyst of the present invention has excellent thermal/mechanical stability in the cracking process, and has less inactivation rate by coke and significantly increases light olefin yield.
摘要翻译：用于生产轻质烯烃的烃蒸汽裂解催化剂，催化剂的制备方法和使用该烯烃的制备方法。更确切地说，本发明涉及通过将CrZrjAkOx（0.5≤j≤120,0≤k≤50）表示的氧化物催化剂粉末混合而成的复合催化剂，A是过渡金属，x是满足根据化合价的条件的数的Cr，Zr和A，以及j和k的值和载体粉末及其烧结，其中氧化物催化剂浸渍在载体上的复合催化剂，以及通过烃蒸汽裂解制备轻质烯烃如乙烯和丙烯的方法在复合催化剂的存在下。本发明的复合催化剂在裂化过程中具有优异的热/机械稳定性，并且焦炭的失活率较低，并显着提高轻烯烃产率。

7. 发明申请

US20120108416A1 CATALYST FOR HYDROCARBON STEAM CRACKING, METHOD OF PREPARING THE SAME AND METHOD OF PREPARING OLEFIN BY USING THE SAME 有权
标题翻译：碳氢化合物破碎用催化剂及其制备方法及使用它们制备烯烃的方法
公开(公告)号：US20120108416A1
公开(公告)日：2012-05-03
申请号：US13309241
申请日：2011-12-01
申请人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-han Kang , Jong-hun Song , Jun-seon Choi , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： B01J21/06 , B01J27/224
CPC分类号： B01J23/26 , B01J21/063 , B01J21/066 , B01J23/002 , B01J35/0033 , B01J37/0009 , B01J37/031 , B01J2523/00 , C07C4/06 , C07C2521/06 , C07C2523/26 , C10G11/02 , C10G11/05 , C10G11/10 , C10G11/16 , C10G11/18 , C10G11/20 , C10G2300/4018 , C10G2400/20 , C07C11/02 , B01J2523/47 , B01J2523/48 , B01J2523/67
摘要： A catalyst for hydrocarbon steam cracking for the production of light olefin, a preparation method of the catalyst and a preparation method of olefin by using the same. More precisely, the present invention relates to a composite catalyst prepared by mixing the oxide catalyst powder represented by CrZrjAkOx (0.5≦j≦120, 0≦k≦50, A is a transition metal, x is the number satisfying the condition according to valences of Cr, Zr and A, and values of j and k) and carrier powder and sintering thereof, a composite catalyst wherein the oxide catalyst is impregnated on a carrier, and a method of preparing light olefin such as ethylene and propylene by hydrocarbon steam cracking in the presence of the composite catalyst. The composite catalyst of the present invention has excellent thermal/mechanical stability in the cracking process, and has less inactivation rate by coke and significantly increases light olefin yield.
摘要翻译：用于生产轻质烯烃的烃蒸汽裂解催化剂，催化剂的制备方法和使用该烯烃的制备方法。更准确地说，本发明涉及通过混合由CrZrjAkOx（0.5＆amp; NlE; j＆nlE; 120,0＆amp; NlE; k＆nlE; 50表示的氧化物催化剂粉末）制备的复合催化剂，A是过渡金属，x是满足根据 Cr，Zr和A的价数，以及j和k的值以及载体粉末及其烧结，其中氧化物催化剂浸渍在载体上的复合催化剂，以及通过烃蒸汽制备轻质烯烃如乙烯和丙烯的方法在复合催化剂存在下开裂。本发明的复合催化剂在裂化过程中具有优异的热/机械稳定性，并且焦炭的失活率较低，并显着提高轻烯烃产率。

8. 发明申请

US20090012340A1 Thermal-cracking method of hydrocarbon 有权
标题翻译：碳氢化合物的热裂解方法
公开(公告)号：US20090012340A1
公开(公告)日：2009-01-08
申请号：US12217246
申请日：2008-07-02
申请人： Jun-seon Choi , Byoung-gi Park , Jin-do Kim , Hyune-jung Ryu
发明人： Jun-seon Choi , Byoung-gi Park , Jin-do Kim , Hyune-jung Ryu
IPC分类号： C07C4/02
CPC分类号： C10G11/04 , C07C4/06 , C07C2523/26 , C10G2300/4018 , C10G2300/807 , C10G2400/20 , Y02P20/124 , C07C11/02
摘要： The present invention relates to a thermal-cracking method of hydrocarbon using a hydrocarbon thermal-cracking apparatus including a tube type furnace having a radiation part for thermally cracking hydrocarbon feedstocks supplied together with steam and a convection part. A hydrocarbon thermal-cracking catalyst is packed in some or entire area of the tube placed in the radiation part of the tube type furnace, wherein the hydrocarbon thermal-cracking catalyst includes an oxide catalyst represented by CrZrjAkOx (wherein, 0.5≦j≦120 and 0≦k≦50, A is a transition metal, and x is a number corresponding to the atomic values of Cr, Zr, and A and the numbers of j and k). Therefore, it is possible to improve yield and selectivity of olefin, reduce fuel consumption due to an excellent heat transfer efficiency and extend decoking interval by reduced production of coke deposited to an inside wall of a tube, in steam cracking of hydrocarbon for producing olefin.
摘要翻译：烃热裂解装置技术领域本发明涉及使用烃热裂解装置的烃热裂解装置，该烃热裂解装置包括具有用于热蒸发与蒸汽一起供应的烃原料的辐射部分和对流部分的管式炉。碳氢化合物热裂解催化剂填充在放置在管式炉的辐射部分中的管的一些或整个区域中，其中烃热裂解催化剂包括由CrZrjAkOx表示的氧化物催化剂（其中，0.5≤j= 120和0 <= k <= 50，A是过渡金属，x是与Cr，Zr和A的原子值对应的数字，以及j和k的数目）。因此，通过在用于生产烯烃的烃的蒸汽裂化中，通过减少沉积到管的内壁的焦炭的产生，可以提高烯烃的产率和选择性，由于优异的传热效率而降低燃料消耗并延长除焦间隔。

9. 发明授权

US5399250A Bipolar electrolyzer 失效
标题翻译：双极电解槽
公开(公告)号：US5399250A
公开(公告)日：1995-03-21
申请号：US121914
申请日：1993-09-17
申请人： Sang Bong Moon , Ju Hwan Jo , Jun Seon Choi , Ho Cheol Shin , Jung Hee Han
发明人： Sang Bong Moon , Ju Hwan Jo , Jun Seon Choi , Ho Cheol Shin , Jung Hee Han
IPC分类号： C25B9/04 , C25B9/18 , C25B9/00 , C25B15/08
CPC分类号： C25B9/045 , C25B9/18
摘要： The present invention relates to an ion exchange membrane type electrolyzer producing chlorine and metal alkali hydroxide. The features include the unit electrolyzer comprises an anode partition wall made of titanium; a cathode partition wall made of nickel; an electrical conduction plate of appropriate dimension for electrical connection; and a current distribution frame. The electrical connection between each unit electrolyzer is provided by spring type metal plates explosively welded.
摘要翻译：本发明涉及一种生产氯和金属氢氧化碱的离子交换膜式电解槽。其特征包括：单元电解槽包括由钛制成的阳极分隔壁; 由镍制成的阴极分隔壁; 用于电气连接的适当尺寸的导电板; 和当前分配框架。每个单元电解槽之间的电气连接由弹性金属板爆炸焊接提供。

10. 发明申请

US20110172483A1 OXIDE CATALYST AND PHOSPHORIC OXIDE CATALYST FOR HYDROCARBON STEAM CRACKING, METHOD FOR PREPARING THE SAME AND METHOD FOR PREPARING OLEFIN BY USING THE SAME 有权
标题翻译：用于碳氢化合物破碎的氧化物催化剂和磷酸氧化物催化剂，其制备方法和使用它们制备烯烃的方法
公开(公告)号：US20110172483A1
公开(公告)日：2011-07-14
申请号：US13072493
申请日：2011-03-25
申请人： Jun-seon CHOI , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
发明人： Jun-seon CHOI , Jun-Han Kang , Jong-hun Song , Byoung-gi Park , Chang-hoon Kang , Si-hyun Noh
IPC分类号： C07C4/06 , B01J21/06 , B01J27/188 , B01J27/19 , B01J27/199 , B01J37/04 , B01J37/03 , B01J37/08 , B01J37/10
CPC分类号： B01J27/188 , B01J21/066 , B01J23/002 , B01J23/26 , B01J23/86 , B01J37/03 , B01J2523/00 , B01J2523/13 , B01J2523/22 , B01J2523/51 , C10G11/04 , C10G2300/4006 , C10G2300/4018 , C10G2300/70 , C10G2300/807 , C10G2400/20 , B01J2523/3712 , B01J2523/48 , B01J2523/67 , B01J2523/47
摘要： The present invention relates to an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking, method for preparing the same and a method for preparing olefin by using the same. More precisely, the present invention relates to an oxide catalyst for hydrocarbon steam cracking represented by formula 1 and a phosphoric oxide catalyst for hydrocarbon steam cracking represented by formula 3 which would be used for the production of olefin such as ethylene and propylene by hydrocarbon steam cracking, and a method for preparing the same. The present invention provides an oxide catalyst and a phosphoric oxide catalyst for hydrocarbon steam cracking that has excellent thermo-stability at high temperature and improved olefin yield. CrZrjAkOx [Formula 1] CrZrjAkPlOx [Formula 3] Wherein, j, k, l and x are as indicated in the description.
摘要翻译：本发明涉及一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其制备方法和使用该方法制备烯烃的方法。更确切地说，本发明涉及由式1表示的烃蒸汽裂解用氧化物催化剂和由式3表示的烃蒸汽裂解用磷酸氧化物催化剂，其用于通过烃蒸汽裂解生产烯烃如乙烯和丙烯，及其制备方法。本发明提供了一种用于烃蒸汽裂化的氧化物催化剂和磷酸盐催化剂，其在高温下具有优异的热稳定性和提高的烯烃产率。 CrZrjAkOx [式1] CrZrjAkP10x [式3]其中，j，k，l和x如说明书中所示。

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