林产化学与工业
林產化學與工業
림산화학여공업
CHEMISTRY AND INDUSTRY OF FOREST PRODUCTS
2014年
6期
29-36
,共8页
樊永胜%蔡忆昔%李小华%俞宁%张蓉仙%尹海云
樊永勝%蔡憶昔%李小華%俞寧%張蓉仙%尹海雲
번영성%채억석%리소화%유저%장용선%윤해운
樟木%真空热解%响应面法%生物油%组分分析
樟木%真空熱解%響應麵法%生物油%組分分析
장목%진공열해%향응면법%생물유%조분분석
camphorwood%vacuum pyrolysis%response surface methodology(RSM)%bio-oil%composition analysis
以樟木木屑为原料,采用真空热解系统进行了制取生物油的中心组合实验研究,以生物油产率为实验指标,利用响应面法( RSM)对热解液化工艺参数进行了优化,并对在最高产率条件下制取的生物油进行了理化特性、傅立叶变换红外光谱( FT-IR)和气质联用( GC-MS)分析。研究结果表明,热解终温、体系压力和升温速率对生物油产率的影响显著,但3者之间的交互作用并不显著。最佳热解工艺条件为:热解终温474.0℃、体系压力7.5 kPa、升温速率20.0℃/min,在此条件下,生物油产率可达50.25%。与预测值(50.41%)较为接近。樟木木屑真空热解所得生物油的含水量较低(21.35%),热值较高(26.82 MJ/kg),常温下的运动黏度为3.85 mm2/s,密度1.08 g/cm3、pH值3.24和残炭量5.54%;生物油成分较为复杂,其中多种有机物可被进一步提取用作工业原料;生物油中羧酸(8.45%)、醛(26.17%)、酮(14.24%)类等腐蚀性和不稳定组分含量较高,需对其进一步精制,以优化真空热解生物油品质,提高其稳定性。
以樟木木屑為原料,採用真空熱解繫統進行瞭製取生物油的中心組閤實驗研究,以生物油產率為實驗指標,利用響應麵法( RSM)對熱解液化工藝參數進行瞭優化,併對在最高產率條件下製取的生物油進行瞭理化特性、傅立葉變換紅外光譜( FT-IR)和氣質聯用( GC-MS)分析。研究結果錶明,熱解終溫、體繫壓力和升溫速率對生物油產率的影響顯著,但3者之間的交互作用併不顯著。最佳熱解工藝條件為:熱解終溫474.0℃、體繫壓力7.5 kPa、升溫速率20.0℃/min,在此條件下,生物油產率可達50.25%。與預測值(50.41%)較為接近。樟木木屑真空熱解所得生物油的含水量較低(21.35%),熱值較高(26.82 MJ/kg),常溫下的運動黏度為3.85 mm2/s,密度1.08 g/cm3、pH值3.24和殘炭量5.54%;生物油成分較為複雜,其中多種有機物可被進一步提取用作工業原料;生物油中羧痠(8.45%)、醛(26.17%)、酮(14.24%)類等腐蝕性和不穩定組分含量較高,需對其進一步精製,以優化真空熱解生物油品質,提高其穩定性。
이장목목설위원료,채용진공열해계통진행료제취생물유적중심조합실험연구,이생물유산솔위실험지표,이용향응면법( RSM)대열해액화공예삼수진행료우화,병대재최고산솔조건하제취적생물유진행료이화특성、부립협변환홍외광보( FT-IR)화기질련용( GC-MS)분석。연구결과표명,열해종온、체계압력화승온속솔대생물유산솔적영향현저,단3자지간적교호작용병불현저。최가열해공예조건위:열해종온474.0℃、체계압력7.5 kPa、승온속솔20.0℃/min,재차조건하,생물유산솔가체50.25%。여예측치(50.41%)교위접근。장목목설진공열해소득생물유적함수량교저(21.35%),열치교고(26.82 MJ/kg),상온하적운동점도위3.85 mm2/s,밀도1.08 g/cm3、pH치3.24화잔탄량5.54%;생물유성분교위복잡,기중다충유궤물가피진일보제취용작공업원료;생물유중최산(8.45%)、철(26.17%)、동(14.24%)류등부식성화불은정조분함량교고,수대기진일보정제,이우화진공열해생물유품질,제고기은정성。
Camphorwood sawdust from industrial processing was treated by vacuum pyrolysis for bio-oil preparation. The response surface methodology ( RSM) was employed to optimize the process for maximum yield of bio-oil. All factors that affected bio-oil yield, including pyrolysis temperature, reaction pressure and heating rate, were investigated. Furthermore, the physicochemical properties of the bio-oil obtained from vacuum pyrolysis at the optimal conditions were evaluated. The chemical composition was also examined using Fourier transform infrared ( FT-IR ) and gas chromatograph/mass spectroscopy ( GC-MS ) . The results showed that these three factors had obvious effects on bio-oil yield. However, the interaction between them was not remarkable. The optimal conditions for bio-oil yield were pyrolysis temperature 474. 0 ℃, reaction pressure 7. 5 kPa and heating rate 20. 0 ℃/min. At this condition, the bio-oil yield could reach 50. 25 % close to 50. 41%—the predicted value. Water content and high heat value of bio-oil was 21. 35% and 26. 82 MJ/kg, and its dynamic viscosity at room temperature, density, pH value and carbon residue content were 3. 85 mm2/s, 1. 08 g/cm3 , 3. 24 and 5. 54%, respectively. Bio-oil from camphorwood sawdust was a complex mixture, which involve aromatics (26.30%), alcohols (12.14%), carboxylic acids (8.45 %), aldehydes (26. 17 %), ketones (14. 24 %) and esters (1. 18%). It also contained some specific organic compounds, which could be further extracted for industrial raw materials. Further study on enhancing the properties of bio-oil should be performed to ensure economic feasibility in future.