燃料化学学报
燃料化學學報
연료화학학보
Journal of Fuel Chemistry and Technology
2015年
10期
1195-1201
,共7页
王洪明%庙荣荣%杨勇%乔玉辉%张琼芳%李春生%黄江平
王洪明%廟榮榮%楊勇%喬玉輝%張瓊芳%李春生%黃江平
왕홍명%묘영영%양용%교옥휘%장경방%리춘생%황강평
碱木质素%超临界水%气化率%碳气化率%气化反应
堿木質素%超臨界水%氣化率%碳氣化率%氣化反應
감목질소%초림계수%기화솔%탄기화솔%기화반응
alkali lignin%supercritical water%gasification efficiency%carbon gasification efficiency%gasification reaction
针对碱木质素难降解的特点,在间歇式反应器中,以Ru/C纳米管为催化剂,对碱木质素在超临界水中的气化进行研究。分别探讨了碱木质素在不同温度、水密度、反应时间、反应浓度、催化剂量的影响,并且分析了Ru/C纳米管催化剂的催化效率。通过单因素实验分析,确定了Ru/C纳米管催化剂催化气化碱木质素的最佳反应条件为,反应温度600℃、水密度0.1284 g/cm3、反应时间60 min、反应质量分数3.0%、催化剂量0.5 g/g(碱木质素)。结果表明,碱木质素在超临界水气化过程中,高温、高水密度(或压力)、长反应时间、低反应物浓度及适量的催化剂将更有利于碱木质素的气化。在最佳反应条件下碱木质素的气化率和碳气化率分别达到73.74%和56.34%,且制氢能力也得到明显提高。
針對堿木質素難降解的特點,在間歇式反應器中,以Ru/C納米管為催化劑,對堿木質素在超臨界水中的氣化進行研究。分彆探討瞭堿木質素在不同溫度、水密度、反應時間、反應濃度、催化劑量的影響,併且分析瞭Ru/C納米管催化劑的催化效率。通過單因素實驗分析,確定瞭Ru/C納米管催化劑催化氣化堿木質素的最佳反應條件為,反應溫度600℃、水密度0.1284 g/cm3、反應時間60 min、反應質量分數3.0%、催化劑量0.5 g/g(堿木質素)。結果錶明,堿木質素在超臨界水氣化過程中,高溫、高水密度(或壓力)、長反應時間、低反應物濃度及適量的催化劑將更有利于堿木質素的氣化。在最佳反應條件下堿木質素的氣化率和碳氣化率分彆達到73.74%和56.34%,且製氫能力也得到明顯提高。
침대감목질소난강해적특점,재간헐식반응기중,이Ru/C납미관위최화제,대감목질소재초림계수중적기화진행연구。분별탐토료감목질소재불동온도、수밀도、반응시간、반응농도、최화제량적영향,병차분석료Ru/C납미관최화제적최화효솔。통과단인소실험분석,학정료Ru/C납미관최화제최화기화감목질소적최가반응조건위,반응온도600℃、수밀도0.1284 g/cm3、반응시간60 min、반응질량분수3.0%、최화제량0.5 g/g(감목질소)。결과표명,감목질소재초림계수기화과정중,고온、고수밀도(혹압력)、장반응시간、저반응물농도급괄량적최화제장경유리우감목질소적기화。재최가반응조건하감목질소적기화솔화탄기화솔분별체도73.74%화56.34%,차제경능력야득도명현제고。
Aiming at the refractory characteristics of alkali lignin, the study on the gasification of alkali lignin in supercritical water was carried out in a batch reactor with Ru/C nanotubes as the catalyst. The effect of temperature, water density, time, concentration of the reactant, catalyst amount on the gasification of alkali lignin was discussed, as well as the catalytic efficiency of the Ru/C catalyst nanotubes. The optimum conditions of the catalytic gasification of alkali lignin on the Ru/C nanotubes obtained with single factor analysis were the reaction temperature of 600 ℃, 0. 128 4 g/cm3 water density, 60 min reaction time, 3. 0% reactant concentration, catalyst amount of 0. 5 g/g (alkali lignin). The results show that during the gasification process of alkali lignin in supercritical water, the high temperature, high water density ( or pressure ) , long reaction time, low reactant concentration and right amount of catalyst will be in favor of the gasification reaction. The alkali lignin gasification efficiency and carbon gasification efficiency reached 73 . 74% and 56 . 34% under the optimal reaction conditions, and the hydrogen production capacity was also significantly improved.