东南大学学报(自然科学版)
東南大學學報(自然科學版)
동남대학학보(자연과학판)
JOURNAL OF SOUTHEAST UNIVERSITY
2014年
4期
782-786
,共5页
王秀文%赵静%董承健%沈德魁%肖睿
王秀文%趙靜%董承健%瀋德魁%肖睿
왕수문%조정%동승건%침덕괴%초예
木质素%结构%TG-FTIR%动力学研究
木質素%結構%TG-FTIR%動力學研究
목질소%결구%TG-FTIR%동역학연구
lignin%structure%TG-FTIR%kinetic analysis
运用元素分析与红外光谱分析仪( FTIR)对Klason法提取的枫木及杉木木质素进行化学结构表征,发现枫木木质素比杉木木质素含有更多的紫丁香酚结构单元。利用热重红外联用分析仪( TG-FTIR)研究了2种木材木质素在动态升温条件下的失重特性及主要气体产物的析出过程,发现木质素热解过程主要分2个阶段,其中枫木木质素为148~268℃及295~494℃两个阶段,杉木木质素则为150~308℃及312~518℃两个阶段。第1个阶段的主要产物是酚类化合物及二氧化碳( CO2),第2个阶段则主要是甲烷以及甲醇的析出,一氧化碳( CO)的生成量也有所增加。基于实验分析,采用一级一阶模型计算枫木、杉木木质素热解2个阶段的动力学参数。
運用元素分析與紅外光譜分析儀( FTIR)對Klason法提取的楓木及杉木木質素進行化學結構錶徵,髮現楓木木質素比杉木木質素含有更多的紫丁香酚結構單元。利用熱重紅外聯用分析儀( TG-FTIR)研究瞭2種木材木質素在動態升溫條件下的失重特性及主要氣體產物的析齣過程,髮現木質素熱解過程主要分2箇階段,其中楓木木質素為148~268℃及295~494℃兩箇階段,杉木木質素則為150~308℃及312~518℃兩箇階段。第1箇階段的主要產物是酚類化閤物及二氧化碳( CO2),第2箇階段則主要是甲烷以及甲醇的析齣,一氧化碳( CO)的生成量也有所增加。基于實驗分析,採用一級一階模型計算楓木、杉木木質素熱解2箇階段的動力學參數。
운용원소분석여홍외광보분석의( FTIR)대Klason법제취적풍목급삼목목질소진행화학결구표정,발현풍목목질소비삼목목질소함유경다적자정향분결구단원。이용열중홍외련용분석의( TG-FTIR)연구료2충목재목질소재동태승온조건하적실중특성급주요기체산물적석출과정,발현목질소열해과정주요분2개계단,기중풍목목질소위148~268℃급295~494℃량개계단,삼목목질소칙위150~308℃급312~518℃량개계단。제1개계단적주요산물시분류화합물급이양화탄( CO2),제2개계단칙주요시갑완이급갑순적석출,일양화탄( CO)적생성량야유소증가。기우실험분석,채용일급일계모형계산풍목、삼목목질소열해2개계단적동역학삼수。
The chemical structure of maple lignin and fir lignin extracted by the Klason method is characterized by the elemental analysis and the Fourier transform infrared spectroscopy ( FTIR) .It is found that lignin from maple contains more syringyl-type groups than that from fir.TG-FTIR ( ther-mogravimetric analyzer coupled with FTIR) is used to examine the characteristics of mass loss and the evolution of typical gaseous product during the dynamic heating process.Pyrolysis of the two lig-nins can be divided into two consecutive mass-loss stages:148 to 268 ℃and 295 to 494 ℃for ma-ple lignin, and 150 to 308 ℃and 312 to 518 ℃for fir lignin, respectively.Phenolic compounds to-gether with carbon dioxid ( CO2 ) are remarkably generated in the first mass-loss stage.While in the second stage, the evolutions of methane and methanol are mainly generated, and carbon monoxide ( CO) is also increased.Based on experimental analyses, a simple one-stage first-order kinetic mod-el is proposed to calculate pyrolysis kinetic parameters of two main pyrolysis stages for maple lignin and fir lignin.