化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
11期
2963-2969
,共7页
高文桂%王华%韩冲%刘文艳%王禹皓%贾淼尧
高文桂%王華%韓遲%劉文豔%王禹皓%賈淼堯
고문계%왕화%한충%류문염%왕우호%가묘요
共沉淀法%助剂%CuO-ZnO-Al2O3%CO2加氢%甲醇
共沉澱法%助劑%CuO-ZnO-Al2O3%CO2加氫%甲醇
공침정법%조제%CuO-ZnO-Al2O3%CO2가경%갑순
co-precipitation%promoter%CuO-ZnO-Al2O3%hydrogenation of CO2%methanol
采用共沉淀法制备了MgO、CaO改性CuO-ZnO-Al2O3催化剂,通过XRD、N2物理吸附-脱附、TG-DTG、H2-TPR、CO2-TPD等表征手段,探讨助剂MgO、CaO添加对催化剂前体物相组成及催化剂微观结构的影响,考察了CO2加氢制备甲醇反应中MgO、CaO改性CuO-ZnO-Al2O3催化剂的性能。结果表明,CaO改性催化剂前体中形成的锌孔雀石相(Cu,Zn)2CO3(OH)2、绿铜锌矿相(Zn,Cu)5(CO3)2(OH)6,促进了催化剂中Cu-Zn协同活性位数量增加,同时助剂CaO的添加降低了催化剂中CuO和ZnO的晶粒度,增大了催化剂比表面积,改善了铜组分的表面分散度,有利于催化剂活性提高;MgO 改性催化剂前体生成了绿铜锌矿相(Zn,Cu)5(CO3)2(OH)6,但没有锌孔雀石相(Cu,Zn)2CO3(OH)2生成,焙烧后催化剂中Cu-Zn协同作用较弱,此外MgO改性后催化剂比表面积减小,催化反应活性降低。MgO、CaO 作为碱性助剂,调变了催化剂表面的碱强度和碱中心浓度,CaO 改性催化剂的表面碱强度大于MgO改性催化剂,与CaO、MgO的碱性强度顺序一致,即CaO>MgO。
採用共沉澱法製備瞭MgO、CaO改性CuO-ZnO-Al2O3催化劑,通過XRD、N2物理吸附-脫附、TG-DTG、H2-TPR、CO2-TPD等錶徵手段,探討助劑MgO、CaO添加對催化劑前體物相組成及催化劑微觀結構的影響,攷察瞭CO2加氫製備甲醇反應中MgO、CaO改性CuO-ZnO-Al2O3催化劑的性能。結果錶明,CaO改性催化劑前體中形成的鋅孔雀石相(Cu,Zn)2CO3(OH)2、綠銅鋅礦相(Zn,Cu)5(CO3)2(OH)6,促進瞭催化劑中Cu-Zn協同活性位數量增加,同時助劑CaO的添加降低瞭催化劑中CuO和ZnO的晶粒度,增大瞭催化劑比錶麵積,改善瞭銅組分的錶麵分散度,有利于催化劑活性提高;MgO 改性催化劑前體生成瞭綠銅鋅礦相(Zn,Cu)5(CO3)2(OH)6,但沒有鋅孔雀石相(Cu,Zn)2CO3(OH)2生成,焙燒後催化劑中Cu-Zn協同作用較弱,此外MgO改性後催化劑比錶麵積減小,催化反應活性降低。MgO、CaO 作為堿性助劑,調變瞭催化劑錶麵的堿彊度和堿中心濃度,CaO 改性催化劑的錶麵堿彊度大于MgO改性催化劑,與CaO、MgO的堿性彊度順序一緻,即CaO>MgO。
채용공침정법제비료MgO、CaO개성CuO-ZnO-Al2O3최화제,통과XRD、N2물리흡부-탈부、TG-DTG、H2-TPR、CO2-TPD등표정수단,탐토조제MgO、CaO첨가대최화제전체물상조성급최화제미관결구적영향,고찰료CO2가경제비갑순반응중MgO、CaO개성CuO-ZnO-Al2O3최화제적성능。결과표명,CaO개성최화제전체중형성적자공작석상(Cu,Zn)2CO3(OH)2、록동자광상(Zn,Cu)5(CO3)2(OH)6,촉진료최화제중Cu-Zn협동활성위수량증가,동시조제CaO적첨가강저료최화제중CuO화ZnO적정립도,증대료최화제비표면적,개선료동조분적표면분산도,유리우최화제활성제고;MgO 개성최화제전체생성료록동자광상(Zn,Cu)5(CO3)2(OH)6,단몰유자공작석상(Cu,Zn)2CO3(OH)2생성,배소후최화제중Cu-Zn협동작용교약,차외MgO개성후최화제비표면적감소,최화반응활성강저。MgO、CaO 작위감성조제,조변료최화제표면적감강도화감중심농도,CaO 개성최화제적표면감강도대우MgO개성최화제,여CaO、MgO적감성강도순서일치,즉CaO>MgO。
CuO-ZnO-Al2O3 was modified by co-precipitation,using MgO,CaO as promoters. The effects of MgO,CaO on phase composition and catalyst structure were illuminated by using N2 adsorption-desorption,TG-DTG,XRD,H2-TPR and CO2-TPD techniques. The catalysts were tested in the synthesis of methanol from CO2 hydrogenation in a fixed-bed reactor. It indicated that the addition of CaO favored the formation of aurichalcite (Zn,Cu)5(CO3)2(OH)6 and malachite zinc (Cu,Zn)2CO3(OH)2 in the precursor of the catalyst. The more (Zn,Cu)5(CO3)2(OH)6 or (Cu,Zn)2CO3(OH)2 precursor possessed,more synergy,lower reduction temperature after calcination it exhibited,which improved the catalytic performance of catalyst modified by CaO. The promoter of MgO did not benefit the formation of aurichalcite (Zn,Cu)5(CO3)2(OH)6 and malachite zinc (Cu,Zn)2CO3(OH)2,which led to less active catalyst due to the weak synergetic effect between Cu and ZnO. On the other hand,the formation of MgO-CuO solid solutions reduced the activity of the catalyst,although the crystallite size of CuO,ZnO was decreased and the dispersion of Cu on the surface was enhanced. It was also found that the intensity and amount of basic sites on the catalyst surface were modulated by the promoter of MgO,CaO. The CaO-modified CuO-ZnO-Al2O3 catalyst possessed stronger basic sites than that of MgO-modified,which was accordance with the basic strength order of CaO and MgO.