-
11.发明授权公开(公告)号：US09950315B2
公开(公告)日：2018-04-24
申请号：US14842301
申请日：2015-09-01
发明人： Rajaram Bal , Rajib Kumar Singha , Chandrashekar Pendem , Laxmi Narayan Siva Kumar Konathala , Ankur Bordoloi , Sandeep Saran
CPC分类号： B01J23/80 , B01J23/002 , B01J35/0013 , B01J35/0093 , B01J37/009 , B01J37/031 , B01J37/036 , B01J37/04 , B01J37/08 , B01J37/10 , B01J2523/00 , C01B3/40 , C01B2203/0238 , C01B2203/1058 , C01B2203/1076 , C01B2203/1241 , Y02P20/142 , Y02P20/52 , B01J2523/22 , B01J2523/27 , B01J2523/847
摘要： The present invention provides a process and catalyst for the production of synthesis gas (a mixture of CO and H2) by reforming of methane with carbon dioxide. The process provides a direct single step selective vapor phase dry reforming of methane with carbon dioxide to produce synthesis gas over Ni—MgO—ZnO catalyst between temperature range of 600° C. to 800° C. at 1 atmospheric pressure. The process provides a methane conversion of 5-95% with H2 to CO mole ratio of 0.83-1.2.
-
公开(公告)号：US09630167B2
公开(公告)日：2017-04-25
申请号：US15093984
申请日：2016-04-08
IPC分类号： C01B3/26 , C01B3/38 , C07C1/02 , B01J23/00 , B01J23/02 , B01J23/06 , B01J23/10 , B01J23/40 , B01J23/42 , B01J23/58 , B01J23/83 , B01J35/00 , B01J35/02 , B01J37/04 , C01B3/40
CPC分类号： B01J23/83 , B01J23/002 , B01J35/0013 , B01J35/002 , B01J35/008 , B01J35/023 , B01J35/08 , B01J37/0018 , B01J37/0236 , B01J37/035 , B01J37/04 , B01J37/088 , B01J2523/00 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0261 , C01B2203/1041 , C01B2203/1058 , C01B2203/1241 , Y02P20/142 , Y02P20/52 , B01J2523/22 , B01J2523/3712 , B01J2523/48 , B01J2523/847
摘要： The present invention provides a Ni nano-cluster supported on MgO—CeO2—ZrO2 catalyst and processes the production of the catalyst. Further, the present invention discloses use of Ni nano-cluster supported on MgO—CeO2—ZrO2 catalyst for the synthesis gas (a mixture of CO and H2) by tri-reforming of methane. The process provides a direct single step selective vapor phase tri-reforming of methane to synthesis gas over NiO—MgO—CeO2—ZrO2 oxide catalyst between temperature range of 600° C. to 800° C. at atmospheric pressure. The process provides a methane conversion of 1-99% with H2 to CO mole ratio of 1.6 to 2.3.
-
13.发明申请Ni Nano Cluster Support on MgO-CeO2-ZrO2 Catalyst for Tri-Reforming of Methane and a Process for Preparation Thereof 有权Ni纳米簇对MgO-CeO2-ZrO2催化剂甲烷三重改性及其制备方法的研究公开(公告)号：US20160296917A1
公开(公告)日：2016-10-13
申请号：US15093984
申请日：2016-04-08
CPC分类号： B01J23/83 , B01J23/002 , B01J35/0013 , B01J35/002 , B01J35/008 , B01J35/023 , B01J35/08 , B01J37/0018 , B01J37/0236 , B01J37/035 , B01J37/04 , B01J37/088 , B01J2523/00 , C01B3/40 , C01B2203/0233 , C01B2203/0238 , C01B2203/0261 , C01B2203/1041 , C01B2203/1058 , C01B2203/1241 , Y02P20/142 , Y02P20/52 , B01J2523/22 , B01J2523/3712 , B01J2523/48 , B01J2523/847
摘要： The present invention provides a Ni nano-cluster supported on MgO—CeO2—ZrO2 catalyst and processes the production of the catalyst. Further, the present invention discloses use of Ni nano-cluster supported on MgO—CeO2—ZrO2 catalyst for the synthesis gas (a mixture of CO and H2) by tri-reforming of methane. The process provides a direct single step selective vapor phase tri-reforming of methane to synthesis gas over NiO—MgO—CeO2—ZrO2 oxide catalyst between temperature range of 600° C. to 800° C. at atmospheric pressure. The process provides a methane conversion of 1-99% with H2 to CO mole ratio of 1.6 to 2.3.
摘要翻译： 本发明提供了一种负载在MgO-CeO 2 -ZrO 2催化剂上的Ni纳米簇，并处理催化剂的生产。 此外，本发明公开了通过甲烷的三重重整使用负载在MgO-CeO 2 -ZrO 2催化剂上的Ni纳米颗粒作为合成气（CO和H 2的混合物）。 该方法在大气压力下，在600℃至800℃的温度范围内，通过NiO-MgO-CeO2-ZrO2氧化物催化剂对甲烷进行合成气的直接单步选择气相三重转化。 该方法提供1-99％的甲烷转化率，H 2与CO摩尔比为1.6至2.3。
-
14.发明申请NANO Ni-Zr OXIDE CATALYST FOR ACTIVATION OF METHANE BY TRI-REFORMING AND A PROCESS FOR THE PREPARATION THEREOF 审中-公开用于通过三次重整反应活化甲烷的纳米镍氧化物催化剂及其制备方法公开(公告)号：US20160289073A1
公开(公告)日：2016-10-06
申请号：US15085697
申请日：2016-03-30
发明人： Rajaram Bal , Rajib Kumar Singha , Ankur Bordoloi , Chandrashekar Pendem , Laxmi narayan Sivakumar Konathala
IPC分类号： C01B3/40 , B01J37/04 , B01J37/03 , B01J23/755
CPC分类号： C01B3/40 , B01J21/066 , B01J23/755 , B01J35/002 , B01J37/0018 , B01J37/031 , B01J37/04 , B01J37/088 , B01J37/16 , C01B2203/0233 , C01B2203/0238 , C01B2203/0244 , C01B2203/0261 , C01B2203/0844 , C01B2203/1041 , C01B2203/1058 , C01B2203/1241 , Y02P20/52
摘要： The present invention provides a Ni—Zr oxide catalyst and a process for the preparation of the catalyst. The invention further provides use of the catalyst for the production of synthesis gas (a mixture of CO and H2) by Tri-reforming of methane. The process provides a direct single step selective vapor phase partial oxidation of methane to synthesis gas over Ni—ZrO2 catalyst between temperature range of 600° C. to 800° C. at atmospheric pressure. The process provides a methane conversion of 1-99% with H2 to CO mole ratio of 1.6 to 2.2.
摘要翻译： 本发明提供了一种Ni-Zr氧化物催化剂及其制备方法。 本发明进一步提供催化剂用于通过甲烷三重转化生产合成气（CO和H 2的混合物）的用途。 该方法在大气压下在600℃至800℃的温度范围内，通过Ni-ZrO 2催化剂提供甲烷直接单步选择性气相部分氧化成合成气。 该方法提供1-99％的甲烷转化率，H 2与CO摩尔比为1.6至2.2。
-
15.发明授权公开(公告)号：US09192923B2
公开(公告)日：2015-11-24
申请号：US14089669
申请日：2013-11-25
发明人： Rajaram Bal , Bipul Sarkar , Chandrasekhar Pendem , Rajib Kumar Singha , Shankha Shubhra Acharyya , Shilpi Ghosh
CPC分类号： B01J29/46 , B01J35/002 , B01J2229/186 , C01B3/40 , C01B2203/0238 , C01B2203/1058 , C01B2203/1082 , C01B2203/1094 , C01B2203/1241 , Y02P20/142 , Y02P20/52
摘要： The present invention provides a coke resistant catalyst and process for sequestration of carbon dioxide via reforming of methane to synthesis gas (a mixture of CO and H2). The process provides a direct single step selective vapor phase carbon dioxide reforming of methane to syngas over gadolinium promoted mesoporous Ni-ZSM catalyst. The process provides almost 11-95% conversion of methane with H2 to CO ratio of 0.82 to 1.
摘要翻译： 本发明提供了一种耐焦炭催化剂和通过将甲烷重整成合成气（CO和H 2的混合物）来封存二氧化碳的方法。 该方法提供了在钆促进的介孔Ni-ZSM催化剂上甲烷到合成气的直接单步选择性气相二氧化碳重整。 该方法提供甲烷几乎11-95％的甲烷转化率，H 2与CO的比例为0.82至1。
-
-
-
-
搜索结果
15 条记录 (耗时 0.028 秒)
