版权说明:本文档由用户提供并上传,收益归属内容提供方,若内容存在侵权,请进行举报或认领
文档简介
1、水、酒精的 饱和蒸汽压水、酒精的 饱和蒸汽压1一,乙醇1一:2二:采用多项式拟合:3二,水41、按温度排列:42. 按压强排列6采用多项式拟合关系,9一,乙醇温度与压力关系如下:(参考资料:化工手册,溶剂手册,物理化学(天津大学四版)温度饱和蒸气压(kPa)-31.50.13-12.00.67-2.31.338.02.6719.05.33205.67126.08.0034.913.334017.39548.426.666046.0163.553.3378.3101.32580108.3290158.27100225.75110314.82120429.92130576.03140758.521
2、50982.851601255.401701581.701801969.851902425.702002958.722103577.492204294.152305109.822406071.39243.16394.62(此为手册的准确值。但是,列出的以外的值缺乏,可以由下面的拟合来补充)乙醇的临界温度为243,临界压力为6.395MPa,沸点(一标准大气压下):78.3 。上述数据,有些整点值没有数据,故可以采用拟合的方式予以补充。一:采用多项式拟合关系,如下:(Y为压力:kPa, X为温度)Y = A*EXP(B*X) -如下图示,R20.9963,准确度较高。但经验证,在135以上时,按
3、拟合较佳。135以下时,有超过10的误差。在下表格中输入温度,可以直接计算任一值:(输入温度值,回车即可)二:采用多项式拟合:采用多项式拟合关系,如下:(Y为压力:kPa, X为温度)Equation: y = A0 + A1*x + A2*x2 + A3*x3 + A4*x4 + A5*x5R2=1A03.27574 A10.09631 A20.0001 A30.00009A41.0308E-6 A51.663E-9R21,准确度更高。在整个区间,拟合结果都较佳。在下表格中输入温度,可以直接计算任一值:二,水饱和水蒸汽表标准:水与对应温度下压力1、按温度排列:温度t/绝对压强p/kPa水蒸汽
4、的密度/kg·m-3焓 H/kJ·kg-1汽化热 r/kJ·kg-1液体水蒸汽00.60820.0048402491.12491.150.87300.0068020.942500.82479.86101.22620.0094041.872510.42468.53151.70680.0128362.802520.52457.7202.33460.0171983.742530.12446.3253.16840.02304104.672539.72435.0304.24740.03036125.602549.32423.7355.62070.03960146.54255
5、9.02412.1407.37660.05114167.472568.62401.1459.58370.06543188.412577.82389.45012.3400.0830209.342587.42378.15515.7430.1043230.272596.72366.46019.9230.1301251.212606.32355.16525.0140.1611272.142615.52343.17031.1640.1979293.082624.32331.27538.5510.2416314.012633.52319.58047.3790.2929334.942642.32307.88
6、557.8750.3531355.882651.12295.29070.1360.4229376.812659.92283.19584.5560.5039397.752668.72270.5100101.330.5970418.682677.02258.4105120.850.7036440.032685.02245.4110143.310.8254460.972693.42232.0115169.110.9635482.322701.32219.0120198.641.1199503.672708.92205.2125232.191.296525.022716.42191.8130270.2
7、51.494546.382723.92177.6135313.111.715567.732731.02163.3140361.471.962589.082737.72148.7145415.722.238610.852744.42134.0150476.242.543632.212750.72118.5160618.283.252675.752762.92037.1170792.594.113719.292773.32054.01801003.55.145763.252782.52019.31901255.66.378807.642790.11982.42001554.777.840852.0
8、12795.51943.52101917.729.567897.232799.31902.52202320.8811.60942.452801.01858.52302798.5913.98988.502800.11811.62403347.9116.761034.562796.81761.82503977.6720.011081.452790.11708.62604693.7523.821128.762780.91651.72705503.9928.271176.912768.31591.42806417.2433.471225.482752.01526.52907443.2939.60127
9、4.462732.31457.43008592.9446.931325.542708.01382.5310 9877.9655.591378.712680.01301.332011300.365.951436.072648.21212.133012879.678.531446.782610.51116.234014615.893.981562.932568.61005.735016 538.5113.21636.202516.7880.536018667.1139.61729.152442.6713.037021040.9171.01888.252301.9411.137422 070.932
10、2.62098.02098.002. 按压强排列绝对压强 p/kPa温度 t/水蒸汽的密度/kg·m-3焓 H/kJ·kg-1汽化热r/kJ·kg-1液体水蒸气1.06.30.0077326.482503.12476.81.512.50.0113352.262515.32463.02.017.00.0148671.212524.22452.92.520.90.0183687.452531.82444.33.023.50.0217998.382536.82438.13.526.10.02523109.302541.82432.54.028.70.02867120.2
11、32546.82426.64.530.80.03205129.002550.92421.95.032.40.03537135.692554.02416.36.035.60.04200149.062560.12411.07.038.80.04864162.442566.32403.88.041.30.05514172.732571.02398.29.043.30.06156181.162574.82393.610.045.30.06798189.592578.52388.915.053.50.09956224.032594.02370.020.060.10.13068251.512606.423
12、54.930.066.50.19093288.772622.42333.740.075.00.24975315.932634.12312.250.081.20.30799339.802644.32304.560.085.60.36514358.212652.12393.970.089.90.42229376.612659.82283.280.093.20.47807390.082665.32275.390.096.40.53384403.492670.82267.4100.099.60.58961416.902676.32259.5120.0104.50.69868437.512684.322
13、46.8140.0109.20.80758457.672692.12234.4160.0113.00.82981473.882698.12224.2180.0116.61.0209489.322703.72214.3200.0120.21.1273493.712709.22204.6250.0127.21.3904534.392719.72185.4300.0133.31.6501560.382728.52168.1350.0138.81.9074583.762736.12152.3400.0143.42.1618603.612742.12138.5450.0147.72.4152622.42
14、2747.82125.4500.0151.72.6673639.592752.82113.2600.0158.73.1686676.222761.42091.1700.0164.03.6657696.272767.82071.5800.0170.44.1614720.962773.72052.7900.0175.14.6525741.822778.12036.21×103179.95.1432762.682782.52019.71.1×103180.25.6333780.342785.52005.11.2×103187.86.1241797.922788.5199
15、0.61.3×103191.56.6141814.252790.91976.71.4×103194.87.1034829.062792.41963.71.5×103198.27.5935843.862794.41950.71.6×103201.38.0814857.772796.01938.21.7×103204.18.5674870.582797.11926.11.8×103206.99.0533883.392798.11914.81.9×103209.89.5392896.212799.21903.02×103
16、212.210.0338907.322799.71892.43×103233.715.00751005.42798.91793.54×103250.320.09691082.92789.81706.85×103263.825.36631146.92776.21629.26×103275.430.84941203.22759.51556.37×103285.736.57441253.22740.81487.68×103294.842.57681299.22720.51403.79×103303.248.89451343.52699.11356.610×103310.955.54071384.02
温馨提示
- 1. 本站所有资源如无特殊说明,都需要本地电脑安装OFFICE2007和PDF阅读器。图纸软件为CAD,CAXA,PROE,UG,SolidWorks等.压缩文件请下载最新的WinRAR软件解压。
- 2. 本站的文档不包含任何第三方提供的附件图纸等,如果需要附件,请联系上传者。文件的所有权益归上传用户所有。
- 3. 本站RAR压缩包中若带图纸,网页内容里面会有图纸预览,若没有图纸预览就没有图纸。
- 4. 未经权益所有人同意不得将文件中的内容挪作商业或盈利用途。
- 5. 人人文库网仅提供信息存储空间,仅对用户上传内容的表现方式做保护处理,对用户上传分享的文档内容本身不做任何修改或编辑,并不能对任何下载内容负责。
- 6. 下载文件中如有侵权或不适当内容,请与我们联系,我们立即纠正。
- 7. 本站不保证下载资源的准确性、安全性和完整性, 同时也不承担用户因使用这些下载资源对自己和他人造成任何形式的伤害或损失。
最新文档
- 2025年安全知识重点题库及答案
- 保洁员岗位考试题及答案
- 2025年城市规划行业智慧城市建设与数字化管理研究报告及未来发展趋势预测
- 2025年软件服务行业云计算技术应用与数据安全研究报告及未来发展趋势预测
- 韵律活动组合试题及答案
- 八上物理高难试卷及答案
- 线缆原材料采购合同模板(3篇)
- 道路交通秩序保障承诺书(5篇)
- 技术团队任务拆分与协作工具
- 《初中化学元素周期表记忆技巧教案》
- 第1章 有理数(压轴必刷30题9种题型专项训练)(原卷版)
- JG-T 191-2006 城市社区体育设施技术要求
- 2024年建筑业10项新技术
- 老年人安全用药与护理PPT
- 保险市场调研报告
- 财务管理中的成本与效益
- 金融信息安全培训
- 老年人营养与健康知识讲座
- 国网公司2021年电网资产统一身份编码物联网标签制作安装指导手册增量分册
- NB-T 47013.8-2012(JB-T 4730.8) 4730.8 承压设备无损检测 第8部分:泄漏检测
- 文言文阅读训练:黄宗羲《续师说》(附答案解析与译文)
评论
0/150
提交评论