应用化工
應用化工
응용화공
APPLIED CHEMICAL INDUSTRY
2014年
12期
2229-2233
,共5页
陈静升%郑化安%张生军%李学强%赵鹤翔%李瑶
陳靜升%鄭化安%張生軍%李學彊%趙鶴翔%李瑤
진정승%정화안%장생군%리학강%조학상%리요
核桃壳%催化热解%动力学%TG-FTIR
覈桃殼%催化熱解%動力學%TG-FTIR
핵도각%최화열해%동역학%TG-FTIR
walnut shell%catalytic pyrolysis%kinetics%TG-FTIR
利用TG-FTIR联用技术研究了升温速率和催化剂(γ-Al2 O3,KCl和USY)对核桃壳热解失重特性和产物生成的影响,并对热解过程进行了动力学分析。结果表明,核桃壳热解主要失重发生在200~450℃,失重78%~82%;升温速率对热解特性的影响较大,随升温速率的增大,核桃壳热解转化率有所降低,热解起始温度及最大失重峰对应的温度向高温侧移动;核桃壳热解符合一级动力学模型,活化能为58~62 kJ/mol。热解的气态产物主要有CO2、H2 O、CO、CH4及酸、醛、酮等羰基化合物,催化剂不仅提高了核桃壳热解的转化率,而且改善热解产物的组成与分布。
利用TG-FTIR聯用技術研究瞭升溫速率和催化劑(γ-Al2 O3,KCl和USY)對覈桃殼熱解失重特性和產物生成的影響,併對熱解過程進行瞭動力學分析。結果錶明,覈桃殼熱解主要失重髮生在200~450℃,失重78%~82%;升溫速率對熱解特性的影響較大,隨升溫速率的增大,覈桃殼熱解轉化率有所降低,熱解起始溫度及最大失重峰對應的溫度嚮高溫側移動;覈桃殼熱解符閤一級動力學模型,活化能為58~62 kJ/mol。熱解的氣態產物主要有CO2、H2 O、CO、CH4及痠、醛、酮等羰基化閤物,催化劑不僅提高瞭覈桃殼熱解的轉化率,而且改善熱解產物的組成與分佈。
이용TG-FTIR련용기술연구료승온속솔화최화제(γ-Al2 O3,KCl화USY)대핵도각열해실중특성화산물생성적영향,병대열해과정진행료동역학분석。결과표명,핵도각열해주요실중발생재200~450℃,실중78%~82%;승온속솔대열해특성적영향교대,수승온속솔적증대,핵도각열해전화솔유소강저,열해기시온도급최대실중봉대응적온도향고온측이동;핵도각열해부합일급동역학모형,활화능위58~62 kJ/mol。열해적기태산물주요유CO2、H2 O、CO、CH4급산、철、동등탄기화합물,최화제불부제고료핵도각열해적전화솔,이차개선열해산물적조성여분포。
The effects of heating rates and catalysts on the pyrolysis characteristics of walnut shell were studied using thermogravimetry analyzer coupled with Fourier transform infrared spectroscopy ( TG-FTIR). The results showed that the main weight loss started at 200 ℃ and ended at 450 ℃,weight loss 78% ~82%. With increasing heating rates,the pyrolysis of walnut shell occurred at a higher temperature and the conversion decreased. FTIR results indicated that main gas products of pyrolysis were CO2 ,H2 O, CO,CH4 ,carbonyl compounds. Kinetic analysis showed that walnut shell pyrolysis could be simplified as a first-order reaction,and calculated activation energy was about 58~62 kJ/mol. Catalytic pyrolysis of wal-nut shell could not only increase the pyrolysis conversion,but also improve the volatiles distribution.