气体的临界流函数C*
点击数：77282012-12-24 10:22:18 来源: 江苏万迅仪表有限公司---官方主页
|
滞带温度/℃ |
滞带压力/MPa |
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|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
100 150 200 250 300 350 400 450 500 550 600 |
0.6735 0.6721 0.6712 0.6700 0.6689 0.6679 0.6667 0.6657 0.6647 0.6639 0.6630 |
0.6795 0.6768 0.6743 0.6725 0.6712 0.6702 0.6691 0.6679 0.6665 0.6648 0.6629 |
0.6855 0.6811 0.6776 0.6752 0.6731 0.6718 0.6704 0.6691 0.6674 0.6657 0.6636 |
0.6918 0.6856 0.6811 0.6777 0.6752 0.6735 0.6718 0.6702 0.6684 0.6665 0.6618 |
0.6985 0.6902 0.6846 0.6803 0.6772 0.6750 0.6732 0.6713 0.6693 0.6673 0.6519 |
0.7056 0.6952 0.6882 0.6830 0.6793 0.6768 0.6745 0.6724 0.6702 0.6679 0.6602 |
0.7129 0.6993 0.6919 0.6857 0.6816 0.6785 0.6760 0.6734 0.6710 0.6686 0.6662 |
0.7030 0.6956 0.6885 0.6837 0.6801 0.6776 0.6745 0.6719 0.6694 0.6668 |
0.7119 0.6997 0.6917 0.6861 0.6820 0.6788 0.6756 0.6729 0.6701 0.6673 |
0.7192 0.7042 0.6948 0.6884 0.6837 0.6802 0.6768 0.6738 0.6708 0.6680 |
0.7261 0.7088 0.6980 0.6907 0.6855 0.6816 0.6794 0.6748 0.6717 0.6686 |
二氧化碳的临界流函数C*
|
滞带温度/℃ |
滞带压力/MPa |
|||||||||||
|
0 |
0.5 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.6739 0.6713 0.6689 0.6668 0.6649 0.6632 0.6616 |
0.6864 0.6797 0.6748 0.6709 0.6679 0.6653 |
0.6918 0.6834 0.6774 0.6728 0.6692 |
0.7032 0.6915 0.6833 0.6772 |
0.7277 0.7077 0.6949 0.6859 |
0.7267 0.7078 0.6952 |
0.7497 0.7222 0.7053 |
0.7783 0.7386 0.7163 |
0.8162 0.7575 0.7282 |
0.7795 0.7412 |
0.8056 0.7555 |
0.8369 0.7713 |
氧的临界流函数C*
|
滞带温度/℃ |
滞带压力/MPa |
|||||||||||
|
0 |
0.5 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.6846 0.6845 0.6844 0.6842 0.6839 0.6835 0.6829 |
0.6886 0.6875 0.6866 0.6859 0.6852 0.6845 0.6837 |
0.6927 0.6905 0.6889 0.6876 0.6865 0.6855 0.6837 |
0.7013 0.6966 0.6934 0.6911 0.6892 0.6876 0.6861 |
0.7104 0.7030 0.6981 0.6946 0.6919 0.6897 0.6877 |
0.7201 0.7096 0.7028 0.6981 0.6945 0.6917 0.6893 |
0.7304 0.7164 0.7076 0.7016 0.6972 0.6938 0.6909 |
0.7413 0.7234 0.7125 0.7052 0.6999 0.6958 0.6925 |
0.7528 0.7307 0.7175 0.7087 0.7025 0.6978 0.6940 |
0.7650 0.7381 0.7225 0.7123 0.7051 0.6998 0.6955 |
0.7779 0.7457 0.7276 0.7159 0.7078 0.7017 0.6970 |
0.7914 0.7535 0.7326 0.7194 0.7103 0.7037 0.6984 |
氩的临界流函数C*
|
滞带温度/℃ |
滞带压力/MPa |
|||||||||||
|
0 |
0.5 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.7262 0.7262 0.7262 0.7262 0.7262 0.7262 0.7262 |
0.7310 0.7297 0.7289 0.7283 0.7279 0.7275 0.7273 |
0.7358 0.7333 0.7316 0.7304 0.7295 0.7289 0.7284 |
0.7460 0.7407 0.7372 0.7347 0.7329 0.7315 0.7035 |
0.7567 0.7482 0.7427 0.7389 0.7362 0.7342 0.7326 |
0.7679 0.7560 0.7484 0.7432 0.7395 0.7367 0.7347 |
0.7797 0.7369 0.7540 0.7474 0.7427 0.7393 0.7367 |
0.7922 0.7720 0.7598 0.7517 0.7460 0.7418 0.7387 |
0.8053 0.7803 0.7655 0.7559 0.7492 0.7443 0.7406 |
0.8191 0.7888 0.7713 0.7601 0.7523 0.7467 0.7426 |
0.8335 0.7975 0.7772 0.7643 0.7555 0.7491 0.7444 |
0.8484 0.8062 0.7830 0.7684 0.7585 0.7515 0.7463 |
空气的临界流函数C*
|
滞止温度/℃ |
滞止压力/MPa |
||||||||||
|
0 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.6850 0.6850 0.6850 0.6850 0.6849 0.6848 0.6847 |
0.6945 0.6900 0.6887 0.6876 0.6870 0.6863 0.6858 |
0.6994 0.6952 0.6925 0.6904 0.6889 0.6878 0.6869 |
0.7069 0.7004 0.6962 0.6927 0.6910 0.6893 0.6880 |
0.7148 7.7059 0.7000 0.6958 0.6930 0.6907 0.6890 |
0.7230 0.7113 0.7038 0.6982 0.6949 0.6921 0.6900 |
0.7316 0.7168 0.7076 0.7011 0.6968 0.6935 0.6910 |
0.7407 0.7224 0.7113 0.7037 0.6987 0.6949 0.6920 |
0.7497 0.7281 0.7150 0.7062 0.7005 0.6961 0.6928 |
0.7588 0.7336 0.7187 0.7087 0.7022 0.6974 0.6937 |
0.7675 0.7391 0.7224 0.7111 0.7039 0.6985 0.6946 |
甲烷的临界流函数
|
滞带温度/℃ |
滞带压力/MPa |
|||||||||||
|
0 |
0.5 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.6726 0.6719 0.6708 0.6694 0.6678 0.6659 0.6639 |
0.6798 0.6771 0.6747 0.6724 0.6701 0.6677 0.6653 |
0.6875 0.6825 0.6787 0.6754 0.6724 0.6695 0.6667 |
0.7048 0.6943 0.6872 0.6817 0.6772 0.6732 0.6696 |
0.7254 0.7075 0.6963 0.6884 0.6822 0.6770 0.6725 |
0.7506 0.7223 0.7061 0.6953 0.6873 0.6808 0.6755 |
0.7827 0.7390 0.7167 0.7026 0.6925 0.6848 0.6784 |
0.8249 0.7581 0.7281 0.7102 0.6980 0.6888 0.6815 |
0.8824 0.7799 0.7404 0.7182 0.7036 0.6929 0.6845 |
0.9576 0.8047 0.7536 0.7266 0.7093 0.6970 0.6876 |
1.0418 0.8324 0.7676 0.7352 0.7151 0.7012 0.6907 |
1.1179 0.8623 0.7823 0.7441 0.7211 0.7054 0.6938 |
氮气的临界流函数C*
|
滞止温度/℃ |
滞止压力/MPa |
|||||||||||
|
0 |
0.5 |
1 |
2 |
3 |
4 |
5 |
6 |
7 |
8 |
9 |
10 |
|
|
－50 －25 0 25 50 75 100 |
0.6848 0.6848 0.6848 0.6848 0.6847 0.6846 0.6845 |
0.6878 0.6869 0.6863 0.6859 0.6855 0.6853 0.6850 |
0.6908 0.6891 0.6879 0.6870 0.6864 0.6859 0.6854 |
0.6970 0.6934 0.6910 0.6893 0.6880 0.6871 0.6863 |
0.7035 0.6978 0.6941 0.6915 0.6896 0.6882 0.6871 |
0.7102 0.7023 0.6972 0.6938 0.6913 0.6894 0.6880 |
0.7171 0.7069 0.7004 0.6960 0.6928 0.6905 0.6888 |
0.7243 0.7115 0.7035 0.6982 0.6944 0.6916 0.6895 |
0.7315 0.7161 0.7067 0.7004 0.6959 0.6927 0.6903 |
0.7389 0.7208 0.7097 0.7025 0.6974 0.6938 0.6910 |
0.7462 0.7254 0.7128 0.7046 0.6989 0.6948 0.6917 |
0.7536 0.7299 0.7158 0.7066 0.7003 0.6958 0.6924 |