高校化学工程学报
高校化學工程學報
고교화학공정학보
JOURNAL OF CHEMICAL ENGINEERING OF CHINESE UNIVERSITIES
2013年
1期
170-173
,共4页
丙酮肟甲醚%饱和蒸气压%摩尔蒸发热%Antoine方程
丙酮肟甲醚%飽和蒸氣壓%摩爾蒸髮熱%Antoine方程
병동우갑미%포화증기압%마이증발열%Antoine방정
acetone oxime methyl ether%saturated vapor pressures%latent heat of vaporization%Antoine equation
采用动态法,利用Rose釜测定了丙酮肟甲醚在307.75~344.05 K的饱和蒸气压,并应用Antoine方程进行关联,获得Antoine常数A、B、C分别为20.64,2338.72和?88.86,Antoine方程计算值与饱和蒸气压实验测定值之间的平均相对误差为0.45%.在此基础上,通过Clausius-Clapeyron方程计算得到丙酮肟甲醚在307.75~344.05 K温度范围内的平均摩尔蒸发热为36479.24 kJ?kmol?1.所得饱和蒸气压方程对丙酮肟甲醚精馏分离过程的设计与操作具有重要意义.
採用動態法,利用Rose釜測定瞭丙酮肟甲醚在307.75~344.05 K的飽和蒸氣壓,併應用Antoine方程進行關聯,穫得Antoine常數A、B、C分彆為20.64,2338.72和?88.86,Antoine方程計算值與飽和蒸氣壓實驗測定值之間的平均相對誤差為0.45%.在此基礎上,通過Clausius-Clapeyron方程計算得到丙酮肟甲醚在307.75~344.05 K溫度範圍內的平均摩爾蒸髮熱為36479.24 kJ?kmol?1.所得飽和蒸氣壓方程對丙酮肟甲醚精餾分離過程的設計與操作具有重要意義.
채용동태법,이용Rose부측정료병동우갑미재307.75~344.05 K적포화증기압,병응용Antoine방정진행관련,획득Antoine상수A、B、C분별위20.64,2338.72화?88.86,Antoine방정계산치여포화증기압실험측정치지간적평균상대오차위0.45%.재차기출상,통과Clausius-Clapeyron방정계산득도병동우갑미재307.75~344.05 K온도범위내적평균마이증발열위36479.24 kJ?kmol?1.소득포화증기압방정대병동우갑미정류분리과정적설계여조작구유중요의의.
Saturated vapor pressures of acetone oxime methyl ether(AOME) were measured in the temperature range of 307.75~344.05 K by dynamic method in a Rose still. The measured saturated vapor pressures and temperatures were correlated by Antoine equation and the constants of equation were determinated as A=20.64, B = 2338.72, and C = ?88.86 by nonlinear regression method. The averaged relative error between saturated vapor pressures calculated from the Antoine equation and the experimental data is 0.45%. Based on the experimental data of vapor pressures, the latent heat of vaporization of acetone oxime methyl ether was also obtained by Clausius-Clapeyron equation and its value is 36479.24 kJ?kmol?1 in the temperature range of 307.75~344.05 K. It is very important to provide the Antoine constants and latent heat of acetone oxime methyl ether for the design and operation of its distillation separation process.