生物质化学工程
生物質化學工程
생물질화학공정
BIOMASS CHEMICAL ENGINEERING
2014年
1期
13-17
,共5页
程毅%邓旭升%刘六军%李瑞
程毅%鄧旭升%劉六軍%李瑞
정의%산욱승%류륙군%리서
生物油%催化酯化%酯化度%反应精馏
生物油%催化酯化%酯化度%反應精餾
생물유%최화지화%지화도%반응정류
Bio-oil%catalytic esterification%esterification degree%reaction rectification
以ZrO2-Al2 O3作为催化剂载体,分别制备了SO2-4/ZrO2-Al2 O3、NaOH/ZrO2-Al2 O3、ZrO2-Al2 O33种固体催化剂,并采用酯化后3A分子筛除水和减压反应精馏两种方法精制生物质裂解油。结果表明,在分别使用SO2-4/ZrO2-Al2 O3, NaOH/ZrO2-Al2 O3,ZrO2-Al2 O33种催化剂的条件下,酯化后3A分子筛除水的方式,可以将产品的含水率降至19.6%、18.3%和15.6%,而反应精馏可以将产品含水率分别降低至4.8%、5.4%和3.8%,较之前者效果更加明显。另外,对于3种不同性质的催化剂,结合酯化度计算式,对催化生物油酯化效果进行评价,可知其催化活性为:SO2-4/ZrO2-Al2 O3>NaOH/ZrO2-Al2 O3>ZrO2-Al2 O3。最后,将得到的油品性质进行检测(包括黏度、pH值、密度和热值等),各项结果表明,使用硫酸化催化剂,并采用减压反应精馏的酯化方式可以制备出一种性能优良的液体燃料。
以ZrO2-Al2 O3作為催化劑載體,分彆製備瞭SO2-4/ZrO2-Al2 O3、NaOH/ZrO2-Al2 O3、ZrO2-Al2 O33種固體催化劑,併採用酯化後3A分子篩除水和減壓反應精餾兩種方法精製生物質裂解油。結果錶明,在分彆使用SO2-4/ZrO2-Al2 O3, NaOH/ZrO2-Al2 O3,ZrO2-Al2 O33種催化劑的條件下,酯化後3A分子篩除水的方式,可以將產品的含水率降至19.6%、18.3%和15.6%,而反應精餾可以將產品含水率分彆降低至4.8%、5.4%和3.8%,較之前者效果更加明顯。另外,對于3種不同性質的催化劑,結閤酯化度計算式,對催化生物油酯化效果進行評價,可知其催化活性為:SO2-4/ZrO2-Al2 O3>NaOH/ZrO2-Al2 O3>ZrO2-Al2 O3。最後,將得到的油品性質進行檢測(包括黏度、pH值、密度和熱值等),各項結果錶明,使用硫痠化催化劑,併採用減壓反應精餾的酯化方式可以製備齣一種性能優良的液體燃料。
이ZrO2-Al2 O3작위최화제재체,분별제비료SO2-4/ZrO2-Al2 O3、NaOH/ZrO2-Al2 O3、ZrO2-Al2 O33충고체최화제,병채용지화후3A분자사제수화감압반응정류량충방법정제생물질렬해유。결과표명,재분별사용SO2-4/ZrO2-Al2 O3, NaOH/ZrO2-Al2 O3,ZrO2-Al2 O33충최화제적조건하,지화후3A분자사제수적방식,가이장산품적함수솔강지19.6%、18.3%화15.6%,이반응정류가이장산품함수솔분별강저지4.8%、5.4%화3.8%,교지전자효과경가명현。령외,대우3충불동성질적최화제,결합지화도계산식,대최화생물유지화효과진행평개,가지기최화활성위:SO2-4/ZrO2-Al2 O3>NaOH/ZrO2-Al2 O3>ZrO2-Al2 O3。최후,장득도적유품성질진행검측(포괄점도、pH치、밀도화열치등),각항결과표명,사용류산화최화제,병채용감압반응정류적지화방식가이제비출일충성능우량적액체연료。
The ZrO2-Al2 O3 was used as a carrier for preparing the catalysts SO2-4 /ZrO2-Al2 O3 , NaOH/ZrO2-Al2 O3 and ZrO2-Al2 O3 in the process of upgrading bio-oil by the methods of dehydration after esterification and reaction recification. Compared these two methods, we could conclude that dehyrating after esterification over 3A molecular sieve could decrease the moisture content to 19. 6%, 18. 3% and 15. 6%, while reaction recification were 4. 8%, 5. 4% and 3. 8% which were better than before under the condition of SO2-4 /ZrO2-Al2 O3 , NaOH/ZrO2-Al2 O3 , ZrO2-Al2 O3 catalyzed, respectively. Meanwhile, according to the evaluation of the bio-oil catalyzed by the modified ZrO2-Al2 O3 with the formula of esterification degree, it indicated the activation of catalysts are SO2-4 /ZrO2-Al2 O3 >NaOH/ZrO2-Al2 O3 >ZrO2-Al2 O3 . Moreover, the quality of the upgraded oil ( kinematics viscosity, pH value, density and heating value ) showed that the bio-oil upgraded by reaction rectification and catalyzed by sulphated metal oxide could produce a out-looking fuel.