农业工程学报
農業工程學報
농업공정학보
2014年
7期
206-211
,共6页
梅德清%谭文兵%张永涛%袁银男
梅德清%譚文兵%張永濤%袁銀男
매덕청%담문병%장영도%원은남
生物柴油%热力学%模型%脂肪酸甲酯%结晶温度%差示扫描量热仪
生物柴油%熱力學%模型%脂肪痠甲酯%結晶溫度%差示掃描量熱儀
생물시유%열역학%모형%지방산갑지%결정온도%차시소묘량열의
biodiesel%thermodynamics%models%fatty acid methyl ester%crystallization temperature%DSC
棕榈酸甲酯(C16:0)、硬脂酸甲酯(C18:0)和油酸甲酯(C18:1)是生物柴油的主要组成部分。为了深入探究生物柴油的结晶行为,该文基于差示扫描量热法(differential scanning calorimetry, DSC)分析了这3种脂肪酸酯的物性参数,研究发现饱和脂肪酸甲酯 C16:0和 C18:0的熔点和熔化焓远远高出不饱和脂肪酸甲酯 C18:1的值,C16:0和C18:0的熔点分别为301.57、310.92 K,C18:1的熔点为255.01 K。对脂肪酸酯组成的二元溶液进行DSC扫描, DSC曲线出现了2个放热峰,并且溶液的结晶点要低于首先析出的饱和脂肪酸酯纯物质时的熔点;随着饱和脂肪酸酯质量分数的增加溶液的结晶点温度也相应提高。将生物柴油当作由多元脂肪酸甲酯的混合溶液时,C16:0和C18:0等饱和脂肪酸甲酯作为溶质,C18:1等不饱和脂肪酸甲酯作为溶剂,建立了热力学模型计算溶液的结晶点温度。将脂肪酸甲酯的混合溶液近似为理想溶液时对此模型进一步简化,并利用简化模型计算得到4种生物柴油的结晶温度,与实测值进行比较得到了很好的验证效果。该研究可为优化生物柴油低温流动性的技术措施提供参考。
棕櫚痠甲酯(C16:0)、硬脂痠甲酯(C18:0)和油痠甲酯(C18:1)是生物柴油的主要組成部分。為瞭深入探究生物柴油的結晶行為,該文基于差示掃描量熱法(differential scanning calorimetry, DSC)分析瞭這3種脂肪痠酯的物性參數,研究髮現飽和脂肪痠甲酯 C16:0和 C18:0的鎔點和鎔化焓遠遠高齣不飽和脂肪痠甲酯 C18:1的值,C16:0和C18:0的鎔點分彆為301.57、310.92 K,C18:1的鎔點為255.01 K。對脂肪痠酯組成的二元溶液進行DSC掃描, DSC麯線齣現瞭2箇放熱峰,併且溶液的結晶點要低于首先析齣的飽和脂肪痠酯純物質時的鎔點;隨著飽和脂肪痠酯質量分數的增加溶液的結晶點溫度也相應提高。將生物柴油噹作由多元脂肪痠甲酯的混閤溶液時,C16:0和C18:0等飽和脂肪痠甲酯作為溶質,C18:1等不飽和脂肪痠甲酯作為溶劑,建立瞭熱力學模型計算溶液的結晶點溫度。將脂肪痠甲酯的混閤溶液近似為理想溶液時對此模型進一步簡化,併利用簡化模型計算得到4種生物柴油的結晶溫度,與實測值進行比較得到瞭很好的驗證效果。該研究可為優化生物柴油低溫流動性的技術措施提供參攷。
종려산갑지(C16:0)、경지산갑지(C18:0)화유산갑지(C18:1)시생물시유적주요조성부분。위료심입탐구생물시유적결정행위,해문기우차시소묘량열법(differential scanning calorimetry, DSC)분석료저3충지방산지적물성삼수,연구발현포화지방산갑지 C16:0화 C18:0적용점화용화함원원고출불포화지방산갑지 C18:1적치,C16:0화C18:0적용점분별위301.57、310.92 K,C18:1적용점위255.01 K。대지방산지조성적이원용액진행DSC소묘, DSC곡선출현료2개방열봉,병차용액적결정점요저우수선석출적포화지방산지순물질시적용점;수착포화지방산지질량분수적증가용액적결정점온도야상응제고。장생물시유당작유다원지방산갑지적혼합용액시,C16:0화C18:0등포화지방산갑지작위용질,C18:1등불포화지방산갑지작위용제,건립료열역학모형계산용액적결정점온도。장지방산갑지적혼합용액근사위이상용액시대차모형진일보간화,병이용간화모형계산득도4충생물시유적결정온도,여실측치진행비교득도료흔호적험증효과。해연구가위우화생물시유저온류동성적기술조시제공삼고。
Biodiesel, as a renewable alternative fuel, is easily crystallized at low temperature, which limits the application of engines fueled with biodiesel. Biodiesel is mainly composed of methyl palmitate (C16:0), methyl stearate (C18:0) and methyl oleate (C18:1). The properties of fuel are closely related to the properties of its compositions, and the fuel properties will change with different mole fraction ratios of some composition. So, it is very important to research the thermal parameters of different compositions. Differential scanning calorimetry (DSC) is a thermo analytical technique by which the difference in the amount of heat required to increase the temperature of a sample and reference is measured as a function of temperature. The result of a DSC experiment is a curve of heat flux related to temperature or time. Through this curve, it is easy to determine transition temperatures and enthalpies, which makes DSC a valuable tool in producing phase diagrams for various chemical systems. Based on the differential scanning calorimeter, thermal parameters of the three methyl esters have been analyzed. The melting point and fusion enthalpy of saturated fatty acid esters (C16:0 and C18:0) are much higher than the ones of unsaturated fatty acid ester (C18:1), the melting points of C16:0, C18:0 and C18:1 are 301.57, 310.92 and 255.01 K, respectively. The binary solution of fatty acid methyl esters has also been scanned, where each curve exhibits two distinct exothermic peaks. These phenomena can be explained in that the high melting point saturated ester precipitated first and the low melting point unsaturated ester precipitated later. Moreover, the crystallization temperature of these solutions is lower than the melting point temperature of the pure saturated fatty acid esters, which precipitated earliest in the solution. It is also clear that the solution crystallization temperature rises accordingly, because the increase of the mass fraction of saturated fatty acid esters. Supposing that biodiesel is a solution combined with different fatty acid methyl esters, the saturated fatty acid esters C16:0 and C18:0 are treated as solutes and the unsaturated fatty acid ester C18:1 is played as solvent, thus the thermodynamic model for calculating the crystallization temperature of the solution has been established. While predicting the crystallization temperature, the solution of fatty acid esters has been dealt with further as an ideal solution;because it just looks at liquid composition as the ideal solution and solid phase composition as not mutually soluble, the model has been simplified. The crystallization temperature of the four different kinds of biodiesel has been calculated by this simplified model, and also has acquired effective verification as compared with the experimental data.