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    气体的临界流函数C*

    点击数:59162012-12-24 10:22:18 来源: 江苏万迅万博体育max首页有限公司---官方主页

    水蒸气的临界流函数C*

    滞带温度/℃

    滞带压力/MPa

    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