欢迎登录材料期刊网

材料期刊网

高级检索

以炭包覆A12O3(CCA)为载体,采用等体积浸渍法制备了17%Ni/CCA催化剂,采用热重-差示量热扫描、扫描电镜、X射线光电子能谱、N2物理吸附、H2程序升温还原和X射线衍射等手段对样品进行了表征,并用于粗1,4-丁二醇加氢反应中.结果表明,炭的引入显著改变了Al2O3的表面性质、负载Ni的存在形态以及金属.载体间的相互作用,因而不同炭含量的Ni/CCA催化剂在粗1,4-丁二醇加氢反应中表现出不同的催化活性.当载体中炭含量为11.6%时,催化剂中的Ni以无定形状态高度分散于载体表面,同时具有适宜的金属.载体相互作用及较好的还原性能,因而其加氢活性最高.

参考文献

[1] Savva P G;Goundani K;Vakros J;Bourikas K Fountzoula C Vattis D Lycourghiotis A Kordulis C .[J].Applied Catalysis B:Environmental,2008,79:199.
[2] Yolcular S;Olgun(O) .[J].Catalysis Today,2008,138:198.
[3] Al-Fatish A S A;Ibrahim A A;Fakeeha A H;Soliman M A Siddiqui M R H Abasaeed A E .[J].Applied Catalysis A:General,2009,364:150.
[4] Aksoylu A E;Onsan Z (I) .[J].Applied Catalysis A:General,1997,164:1.
[5] Suzdorf A R;Morozov S V;Anshits N N;Tsignova S I Anshits A G .[J].Catalysis Letters,1994,29:49.
[6] Hernández S;Solarino L;Orsello G;Russo N Fino D Saracco G Specchia V .[J].International Journal of Hydrogen Energy,2008,33:3209.
[7] Wang H;Fan Y;Shi G;Liu Z H Liu H Y Bao X J .[J].Catalysis Today,2007,125:149.
[8] Zhang Y H;Xiong G X;Sheng Sh Sh;Yang W Sh .[J].Catalysis Today,2000,63:517.
[9] Ryczkowski J;Borowiecki T .[J].Reaction Kinetics and Catalysis Letters,1993,49:127.
[10] Hoffer B W;Van Langeveld A D;Janssens J P;Bonné R L C Lok C M Moulijn J A .[J].Journal of Catalysis,2000,192:432.
[11] Chang Z X;Zhao X G;Li J L;Zhu Q M .[J].Applied Catalysis A:General,2001,205:31.
[12] Xu Z.;Zhang JY.;Chang L.;Zhou RQ.;Duan ZT.;Li YM. .Bound-state Ni species - a superior form in Ni-based catalyst for CH4/CO2 reforming[J].Applied Catalysis, A. General: An International Journal Devoted to Catalytic Science and Its Applications,2001(1/2):45-53.
[13] Tsyganok A I;Tsunoda T;Hamakawa S;Suzuki K Takehira K Hayakawa T .[J].Journal of Catalysis,2003,213:191.
[14] Guo J J;Lou H;Zhao H;Chai D F Zheng X M .[J].Applied Catalysis A:General,2004,273:75.
[15] Hou Z Y;Yashima T .[J].Applied Catalysis A:General,2004,261:205.
[16] Takehira K;Shishido T;Wang P;Kosaka T Takaki K .[J].Journal of Catalysis,2004,221:43.
[17] 刘勇 .[D].太原:中国科学院山西煤炭化学研究所,2005.
[18] Li G H;Hu L J;Hill J M .[J].Applied Catalysis A:General,2006,301:16.
[19] Velu S;Gangwal SK .Synthesis of alumina supported nickel nanoparticle catalysts and evaluation of nickel metal dispersions by temperature programmed desorption[J].Solid state ionics,2006(7/8):803-811.
[20] 郝志显,李全芝.混合硝酸镍和醋酸镍制备的催化剂的特征和催化加氢抗硫性能[J].化学学报,2002(07):1339-1345.
[21] Burattin P;Che M;Louis C .[J].Journal of Physical Chemistry B,1998,102:2722.
[22] Lok C M .[P].US 6 673 743,2004.
[23] Lin L;Lin W;Zhu YX;Zhao BY;Xie YC;Jia GQ;Li C .Uniformly carbon-covered alumina and its surface characteristics[J].Langmuir: The ACS Journal of Surfaces and Colloids,2005(11):5040-5046.
[24] 刘金河,杨普江,张景峰,马淑杰.覆炭载体镍催化剂脱氢活性和表面酸性研究[J].石油化工,2004(04):330-334.
[25] He S B;Sun Ch L;Du H Zh;Dai X H Wang B .[J].Chemical Engineering Journal,2008,141:284.
[26] Zheng M Y;Shu Y Y;Sun J;Zhang T .[J].Catalysis Letters,2008,121:90.
[27] 梁旭,李海涛,张因,赵永祥,孙自瑾,梁小元.载体孔结构对丁炔二醇二段加氢Ni/γ-Al2O3催化剂加氢性能的影响[J].分子催化,2009(03):209-214.
[28] 徐亚琳,李海涛,张建平,王永钊,赵永祥.临氢水热处理对Ni/γ-Al2O3催化剂结构和性能的影响[J].分子催化,2010(02):112-116.
[29] Bokhimi X;Toledo-Antonio J A;Guzmán-Castillo M L;Mar-Mar B Hernández-Beltrán F Navarrete J .[J].Journal of Solid State Chemistry,2001,161:319.
[30] 沈曾民;张文辉;张学军.活性炭材料的制备与应用[M].北京:化学工业出版社,2006:3.
[31] Sahoo S K;Rao P V C;Rajeshwer D;Krishnamarthy K R Singh I D .[J].Applied Catalysis A:General,2003,244:311.
[32] 章青,王会芳,孙果宋,黄科林,方维平,杨意泉.活性炭材料对镍基催化剂乙醇气相羰化性能的影响[J].催化学报,2009(06):555-559.
[33] 刘金红,张倩,姚虎卿.Ni/AC催化剂的分散阈值及阈值效应[J].催化学报,2006(12):1139-1143.
[34] Chary K V R;Rao P V R;Rao V V .[J].Catalyst Communication,2008,9:886.
[35] Kim P;Kim H;Joo JB;Kim W;Song IK;Yi J .Effect of nickel precursor on the catalytic performance of Ni/Al2O3 catalysts in the hydrodechlorination of 1,1,2-trichloroethane[J].Journal of molecular catalysis, A. Chemical,2006(1/2):178-183.
上一张 下一张
上一张 下一张
计量
  • 下载量()
  • 访问量()
文章评分
  • 您的评分:
  • 1
    0%
  • 2
    0%
  • 3
    0%
  • 4
    0%
  • 5
    0%