水热沉淀法制备NiO-CaO/Al2O3复合催化剂及其在ReSER制氢中的应用Preparation of a NiO-CaO/Al2O3 Sorption Complex Catalyst by Hydrothermal Precipitation Method and its Application in ReSER Process
张帆,吴嵘,吴素芳
摘要(Abstract):
制备了一组高催化活性的NiO-CaO/Al2O3复合催化剂并将其应用于反应吸附强化甲烷水蒸气重整制氢(ReSER)过程中。采用水热沉淀法制备了具有层状复合金属氢氧化物结构(NiAl-LDHs)的复合催化剂前驱体,高温焙烧后得到NiO-CaO/Al2O3复合催化剂hd-cat。通过传统浸渍法制备了另一组相同组分含量的NiO-CaO/Al2O3复合催化剂ci-cat作为对比。BET测得催化剂hd-cat比表面积为134.4 m2·g-1,H2-TPD测得其Ni金属分散度为9.25%,分别为催化剂ci-cat的3.8倍和1.3倍。CO2反应吸附性能(TGA)测试结果表明hd-cat吸附容量和吸附速率分别是ci-cat的1.8倍和2.7倍。在固定床反应器上,反应压力0.1 MPa、温度600℃、H2O/CH4摩尔比4:1条件下,评价了不同体积空速下复合催化剂ReSER制氢效果。hd-cat能达到的最大体积空速为2376 h-1,在此条件下能得到94.4%浓度的H2和98.4%的CH4转化率,十次反应-再生循环中,H2浓度和CH4转化率均保持在90%以上。相同反应条件下,复合催化剂ci-cat在体积空速1188 h-1时便失去制氢活性。实验结果证明水热沉淀法制备的高活性的复合催化剂hd-cat能适于高空速下的ReSER循环制氢要求。
关键词(KeyWords): 氢气;Ni基催化剂;水热沉淀法;氧化钙
基金项目(Foundation): 国家自然科学基金(20876142)
作者(Author): 张帆,吴嵘,吴素芳
参考文献(References):
- [1]Simpson A P,Lutz A E.Exergy analysis of hydrogen production via steam methane reforming[J].Int J Hydrogen Energy,2007,32(18):4811-4820.
- [2]Balasubramanian B,Lopez Ortiz A,Kaytakoglu S,et al.Hydrogen from methane in a single-step process[J].Chem Eng Sci,1999,54(15-16):3543-3552.
- [3]Ding Y,Alpay E.Adsorption-enhanced steam-methane reforming[J].Chem Eng Sci,2000,55(18):3929-3940.
- [4]Xiu G,Li P,Rodrigues A E.Adsorption-enhanced steam-methane reforming with intraparticle-diffusion limitations[J].Chem Eng J,2003,95(1-3):83-93.
- [5]Harrison D P.Sorption-enhanced hydrogen production:a review[J].Ind Eng Chem Res,2008,47(17):6486-6501.
- [6]Wu S F,Li L B,Zhu Y Q,et al.A micro-sphere catalyst complex with nano CaCO3 precursor for hydrogen production used in ReSER process[J].Eng Sci,2010,8(1):22-26.
- [7]HE Juan(贺隽).Study on the complex catalyst and kinetics in the adsorption enhanced reforming for hydrogen production(吸附强化甲烷水蒸汽重整制氢的复合催化剂及反应动力学研究)[D].Hangzhou(杭州):Zhejiang University(浙江大学),2007.
- [8]Satrio J A,Shanks B H,Wheelock T D.Development of a novel combined catalyst and sorbent for hydrocarbon reforming[J].Ind Eng Chem Res,2005,44(11):3901-3911.
- [9]Satrio J A,Shanks B H,Wheelock T D.A combined catalyst and sorbent for enhancing hydrogen production from coal or biomass[J].Energy Fuels,2007,21(1):322-326.
- [10]Albrecht K O,Satrio J A,Shanks B H,et al.Application of a combined catalyst and sorbent for steam reforming of methane[J].Ind Eng Chem Res,2010,49(9):4091-4098.
- [11]Martavaltzi C S,Lemonidou A A.Hydrogen production via sorption enhanced reforming of methane:Development of a novel hybrid material—reforming catalyst and CO2 sorbent[J].Chem Eng Sci,2010,65(14):4134-4140.
- [12]Kim J,Ko C H,Yi K B.Sorption enhanced hydrogen production using one-body CaO-Ca12Al14O33-Ni composite as catalytic absorbent[J].Int J Hydrogen Energy,2013,14(38):6072-6078.
- [13]Wu G,Zhang C,Li S,et al.Sorption enhanced steam reforming of ethanol on Ni-CaO-Al2O3 multifunctional catalysts derived from hydrotalcite-like compounds[J].Energy&Environment Sci,2012(5):8942-8949.
- [14]Broda M,Kierzkowska A M,Baudouin D,et al.Sorbent-enhanced methane reforming over a Ni-Ca-Based,bifunctional catalyst sorbent[J].ACS Catal,2012,2(8):1635-1646.
- [15]Chanburanasiri N,Ribeiro A M,Rodrigues A E,et al.Hydrogen production via sorption enhanced steam methane reforming process using Ni/CaO multifunctional catalyst[J].Ind Eng Chem Res,2011,50(24):13662-13671.
- [16]Wu S F,Wang L L.Improvement of the stability of a ZrO2-modified Ni-nano-CaO sorption complex catalyst for ReSER hydrogen production[J].Int J Hydrogen Energy,2010,35(13):6518-6524.
- [17]Feng H Z,Lan P Q,Wu S F.A study on the stability of a NiO-CaO/Al2O3 complex catalyst by La2O3 modification for hydrogen production[J].Int J Hydrogen Energy,2012,37(19):14161-14166.
- [18]Andonova S,Vladov C,Pawelec B,et al.Effect of the modified supportγ-Al2O3-CaO on the structure and hydrodesulfurization activity of Mo and Ni-Mo catalysts[J].Appl Catal,A,2007,328(2):201-209.
- [19]Liu S,Guan L,Li J,et al.CO2 reforming of CH4 over stabilized mesoporous Ni-CaO-ZrO2 composites[J].Fuel,2008,87(12):2477-2481.
- [20]Zhang L,Liu J,Li W,et al.Ethanol steam reforming over Ni-Cu/Al2O3-MyOz(M=Si,La,Mg,and Zn)catalysts[J].J Nat Gas Chem,2009,18(1):55-65.
- [21]Sun N,Wen X,Wang F,et al.Effect of pore structure on Ni catalyst for CO2 reforming of CH4[J].Energy&Environment Sci,2010,3(3):366-369.
- [22]Feng J T,Lin Y J,Evans D G,et al.Enhanced metal dispersion and hydrodechlorination properties of a Ni/Al2O3 catalyst derived from layered double hydroxides[J].J Catal,2009,266(2):351-358.
- [23]Yang R,Wu J,Li X,et al.Hydrotreating of crude 2-ethylhexanol over Ni/Al2O3 catalysts:Influence of the Ni oxide dispersion on the active sites[J].Appl Catal,A,2010,383(1-2):112-118.
- [24]Centi G,Perathoner S.Catalysis by layered materials:A review[J].Microporous Mesoporous Mater,2008,107(1):3-15