Propiedades de mezclas binarias a diferentes temperaturas (Tabla 2) | Exámenes selectividad de Fundamentos de Administración y Gestión

Table 2. Refractive Indices, Changes of Refractive Indices, Densities (

*

cmg

)

and excess molar volumes (

13 

molcm

) of Binary Mixtures at Different

Temperatures

n



n



Ethanol(1)+Hexane(2)

293.15 K

Ethanol(1)+Heptane(2)

293.15 K

0.0000

0.1147

0.2055

0.3054

0.4017

0.4960

0.5992

0.7004

0.7991

0.9002

1.0000

1.3762

1.3751

1.3741

1.3730

1.3719

1.3706

1.3690

1.3673

1.3655

1.3636

1.3618

0.0000

0.0006

0.0009

0.0012

0.0015

0.0014

0.0012

0.0008

0.0004

0.0000

0.6598

0.6661

0.6719

0.6791

0.6873

0.6968

0.7091

0.7237

0.7410

0.7625

0.7895

0.0000

0.1457

0.2297

0.3191

0.3579

0.3553

0.3249

0.2620

0.1770

0.1036

0.0000

0.1005

0.2049

0.3050

0.4063

0.5035

0.6007

0.7043

0.8014

0.9032

1.0000

1.3896

1.3885

1.3868

1.3850

1.3827

1.3802

1.3772

1.3736

1.3702

1.3664

1.3618

0.0000

0.0017

0.0029

0.0039

0.0044

0.0046

0.0043

0.0036

0.0029

0.0019

0.0000

0.6838

0.6873

0.6919

0.6972

0.7038

0.7114

0.7205

0.7325

0.7466

0.7658

0.7895

0.0000

0.2024

0.3234

0.3987

0.4157

0.4039

0.3767

0.3171

0.2396

0.1124

0.0000

298.15 K

0.0000

0.1147

0.2055

0.3054

0.4017

0.4960

0.5992

0.7004

0.7991

0.9002

1.0000

1.3745

1.3731

1.3720

1.3708

1.3697

1.3685

1.3669

1.3652

1.3636

1.3620

1.3604

0.0000

0.0002

0.0004

0.0006

0.0009

0.0010

0.0008

0.0006

0.0004

0.0002

0.0000

0.6552

0.6615

0.6673

0.6745

0.6827

0.6922

0.7045

0.7191

0.7363

0.7580

0.7853

0.0000

0.1502

0.2362

0.3280

0.3699

0.3692

0.3402

0.2794

0.2067

0.1176

0.0000

0.1005

0.2049

0.3050

0.4063

0.5035

0.6007

0.7043

0.8014

0.9032

1.0000

1.3863

1.3852

1.3837

1.3820

1.3799

1.3776

1.3748

1.3714

1.3682

1.3645

1.3604

0.0000

0.0015

0.0027

0.0036

0.0041

0.0043

0.0041

0.0033

0.0027

0.0016

0.0000

0.6797

0.6831

0.6877

0.6929

0.6994

0.7070

0.7160

0.7279

0.7419

0.7615

0.7853

0.0000

0.2194

0.3407

0.4322

0.4602

0.4429

0.4233

0.3682

0.2926

0.1198

0.0000

303.15 K

0.0000

0.1147

0.2055

0.3054

0.4017

0.4960

0.5992

0.7004

0.7991

0.9002

1.0000

1.3716

1.3702

1.3691

1.3679

1.3667

1.3655

1.3642

1.3628

1.3614

1.3598

1.3582

0.0000

0.0001

0.0003

0.0004

0.0005

0.0006

0.0005

0.0003

0.0000

0.6504

0.6566

0.6622

0.6695

0.6777

0.6874

0.6999

0.7147

0.7319

0.7538

0.7814

0.0000

0.1775

0.3054

0.3841

0.4298

0.4048

0.3577

0.2830

0.2224

0.1284

0.0000

0.1005

0.2049

0.3050

0.4063

0.5035

0.6007

0.7043

0.8014

0.9032

1.0000

1.3836

1.3824

1.3810

1.3793

1.3772

1.3749

1.3722

1.3691

1.3659

1.3623

1.3582

0.0000

0.0014

0.0026

0.0034

0.0039

0.0041

0.0039

0.0034

0.0027

0.0016

0.0000

0.6755

0.6789

0.6834

0.6886

0.6951

0.7023

0.7117

0.7237

0.7377

0.7571

0.7814

0.0000

0.2263

0.3685

0.4616

0.4909

0.4830

0.4551

0.3837

0.3150

0.1617

0.0000

308.15 K

0.0000

0.1147

0.2055

0.3054

0.4017

0.4960

0.5992

0.7004

0.7991

0.9002

1.3687

1.3672

1.3661

1.3649

1.3638

1.3628

1.3615

1.3602

1.3589

1.3575

0.0000

-0.0001

0.0000

0.0001

0.0003

0.0004

0.0003

0.0001

0.6460

0.6516

0.6573

0.6645

0.6728

0.6824

0.6949

0.7096

0.7269

0.7488

0.0000

0.2879

0.3866

0.4701

0.4875

0.4651

0.4031

0.3225

0.2403

0.1333

0.0000

0.1005

0.2049

0.3050

0.4063

0.5035

0.6007

0.7043

0.8014

0.9032

1.3809

1.3799

1.3783

1.3765

1.3745

1.3722

1.3696

1.3665

1.3632

1.3599

0.0000

0.0015

0.0025

0.0032

0.0037

0.0038

0.0036

0.0031

0.0022

0.0014

0.6711

0.6742

0.6787

0.6840

0.6904

0.6979

0.7068

0.7185

0.7324

0.7516

0.0000

0.2866

0.4198

0.4855

0.5227

0.5104

0.4939

0.4495

0.3689

0.2139

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Table 2. Refractive Indices, Changes of Refractive Indices, Densities (



g cm )

cm  mol ) of Binary Mixtures at Different

Temperatures

x 1 nD  nD

 E

VM x 1 nD  nD

 E

VM

Ethanol(1)+Hexane(2) 293.15 K

Ethanol(1)+Heptane(2)

Table 2. (Continued)

x 1 nD  nD  E VM x 1 nD  nD  E

VM

Ethanol(1)+Octane(2) 293.15 K Ethanol(1)+water(2)

The correlation parameters and the root-mean-square deviations ( ) calculated

using eqs3 are listed in Table 3. This deviation is calculated by applying the

 - 3  and excess molar volumes (

1. 293.15 K
- 1. - - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. 298.15 K 298.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. 303.15 K 303.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. 308.15 K 308.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - -0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1.0000 1.3561 0.0000 0.7763 0.0000 1.0000 1.3561 0.0000 0.7763 0. - 0. 293.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - -0. - -0. - -1. - -1. - -1. - -0. - -0. - -0. - -0. - 0. - 0. 298.15 K 298.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - -0. - -0. - -1. - -1. - -1. - -0. - -0. - -0. - -0. - 0. - 0. 303.15 K 303.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - -0. - -0. - -1. - -1. - -1. - -0. - -0. - -0. - -0. - 0. - 0. 308.15 K 308.15 K - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 1. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - 0. - -0. - -0. - -1. - -1. - -1. - -0. - -0. - -0. - -0. - 0.

Propiedades de mezclas binarias a diferentes temperaturas (Tabla 2), Exámenes selectividad de Fundamentos de Administración y Gestión

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Table 2. Refractive Indices, Changes of Refractive Indices, Densities (

g cm )

cm  mol ) of Binary Mixtures at Different

Temperatures

x 1 nD  nD

 E

VM x 1 nD  nD

 E

VM

Table 2. (Continued)

VM

The correlation parameters and the root-mean-square deviations ( ) calculated