东北林业大学学报
東北林業大學學報
동북임업대학학보
JOURNAL OF NORTHEAST FORESTRY UNIVERSITY
2013年
8期
122-125,154
,共5页
郑云武%黄元波%郑志锋%顾继友
鄭雲武%黃元波%鄭誌鋒%顧繼友
정운무%황원파%정지봉%고계우
橡胶籽壳%热化学液化%多元醇%动力学
橡膠籽殼%熱化學液化%多元醇%動力學
상효자각%열화학액화%다원순%동역학
Rubber seed shell%Thermochemical liquefaction%Polyhydric alcohol%Kinetics
以聚乙二醇/丙三醇( m(聚乙二醇)∶m(丙三醇)=4∶1)为液化剂,研究了硫酸催化橡胶籽壳粉在多元醇体系的液化反应,探讨了不同反应因素对液化反应的影响,同时通过反应时间与液化率的关系,揭示了液化产物的性质随反应时间变化的规律。结果表明:当催化剂用量为8%、反应温度150℃、V (液化剂)∶m (橡胶籽壳)=4 mL∶1 g、液化反应时间90 min时,其液化产率高达94.32%。同时,橡胶籽壳液化符合二级动力学反应,活化能Ea=20.60 kJ/mol,指前因子A=3.6598 s-1,ΔH=17.09 kJ/mol,ΔS=-245.34 J/mol,ΔG=120.91 kJ/mol,表明体系较易进行,在外界供能的前提下,体系的有序性发生了变化,反应形成了某种形式的协同的过渡态,体系变得复杂。
以聚乙二醇/丙三醇( m(聚乙二醇)∶m(丙三醇)=4∶1)為液化劑,研究瞭硫痠催化橡膠籽殼粉在多元醇體繫的液化反應,探討瞭不同反應因素對液化反應的影響,同時通過反應時間與液化率的關繫,揭示瞭液化產物的性質隨反應時間變化的規律。結果錶明:噹催化劑用量為8%、反應溫度150℃、V (液化劑)∶m (橡膠籽殼)=4 mL∶1 g、液化反應時間90 min時,其液化產率高達94.32%。同時,橡膠籽殼液化符閤二級動力學反應,活化能Ea=20.60 kJ/mol,指前因子A=3.6598 s-1,ΔH=17.09 kJ/mol,ΔS=-245.34 J/mol,ΔG=120.91 kJ/mol,錶明體繫較易進行,在外界供能的前提下,體繫的有序性髮生瞭變化,反應形成瞭某種形式的協同的過渡態,體繫變得複雜。
이취을이순/병삼순( m(취을이순)∶m(병삼순)=4∶1)위액화제,연구료류산최화상효자각분재다원순체계적액화반응,탐토료불동반응인소대액화반응적영향,동시통과반응시간여액화솔적관계,게시료액화산물적성질수반응시간변화적규률。결과표명:당최화제용량위8%、반응온도150℃、V (액화제)∶m (상효자각)=4 mL∶1 g、액화반응시간90 min시,기액화산솔고체94.32%。동시,상효자각액화부합이급동역학반응,활화능Ea=20.60 kJ/mol,지전인자A=3.6598 s-1,ΔH=17.09 kJ/mol,ΔS=-245.34 J/mol,ΔG=120.91 kJ/mol,표명체계교역진행,재외계공능적전제하,체계적유서성발생료변화,반응형성료모충형식적협동적과도태,체계변득복잡。
The research was conducted to study the rubber seed shell liquefied reaction in polyol system to explore the liquefied reaction influence on different reaction conditions by using polyethylene glycol/glycerol as liquefied agent and sulfuric acid as catalysis.With the relation between the reaction time and the liquefaction ratio, the rule concerning the variation of liq-uefied product properties was revealed with reaction time changing .When the catalysis accounts for 8%, the reaction tem-perature is150 ℃, the rate of liquid to raw material is 4 ∶1 and the reaction time is 90 min and the liquation ratio can reach up to 94.32%.The liquefaction of rubber seed shell meets up with the rule of second order kinetics reaction.The activation energy Ea=20.60 KJ/mol, the pre-exponential factor A=3.659 8 s-1 ,ΔH=17.09 kJ/mol,ΔS=-245.34 J/mol and ΔG=120.91 kJ/mol.Therefore, the experimental system can be operated easily.Outside energy supply, the experimental system ordering changes, the reaction forms a kind of concerted transition state, and the system becomes complicated.