Table 2 Particle mobility calculated for studied generalised LJ systems (in normalised units) and for ethane (in K and \(nm^2 / (\mu s \cdot K)\) and \({\tilde{\mu }}=\mu \sqrt{\varepsilon M/\sigma ^2}\), where \(M=30.07\,g/mol\) is ethane molar mass).

From: Diffusion mobility increases linearly on liquid binodals above triple point

LJ12-4

T

1.788

2.012

2.247

2.463

2.687

2.912

3.137

3.318

3.412

3.507

3.601

3.696

3.790

3.884

\(\rho\)

0.944

0.914

0.882

0.850

0.819

0.783

0.749

0.719

0.703

0.687

0.670

0.653

0.635

0.617

\(\mu\)

0.031

0.039

0.048

0.056

0.065

0.075

0.085

0.093

0.097

0.103

0.108

0.113

0.119

0.124

T

4.073

4.168

4.262

4.309

4.368

4.426

4.485

4.544

4.602

4.661

4.720

4.778

4.837

\(\rho\)

0.578

0.558

0.536

0.525

0.510

0.495

0.479

0.461

0.443

0.422

0.398

0.369

0.322

\(\mu\)

0.137

0.144

0.154

0.159

0.163

0.172

0.178

0.186

0.198

0.208

0.223

0.246

0.286

LJ12-5

T

1.032

1.160

1.288

1.416

1.544

1.672

1.704

1.739

1.773

1.808

1.842

1.877

1.911

1.946

\(\rho\)

0.867

0.833

0.797

0.761

0.723

0.680

0.670

0.658

0.647

0.634

0.622

0.608

0.594

0.579

\(\mu\)

0.041

0.054

0.068

0.082

0.096

0.115

0.119

0.124

0.130

0.134

0.142

0.147

0.152

0.161

T

2.00

2.026

2.049

2.071

2.094

2.117

2.140

2.162

\(\rho\)

0.552

0.539

0.525

0.511

0.494

0.475

0.451

0.416

\(\mu\)

0.175

0.181

0.191

0.198

0.208

0.221

0.238

0.269

LJ12-6

T

0.721

0.748

0.774

0.801

0.829

0.856

0.882

0.909

0.936

0.964

0.991

1.008

1.024

1.039

\(\rho\)

0.832

0.821

0.808

0.796

0.784

0.772

0.758

0.745

0.733

0.717

0.704

0.694

0.685

0.676

\(\mu\)

0.053

0.058

0.064

0.070

0.076

0.081

0.089

0.095

0.100

0.109

0.116

0.121

0.126

0.130

T

1.070

1.085

1.100

1.116

1.131

1.146

1.161

1.172

1.185

1.198

1.211

1.224

1.237

1.250

\(\rho\)

0.658

0.649

0.639

0.629

0.618

0.606

0.594

0.586

0.574

0.562

0.549

0.534

0.518

0.500

\(\mu\)

0.141

0.145

0.150

0.156

0.163

0.170

0.177

0.183

0.189

0.198

0.206

0.216

0.226

0.240

T

1.276

\(\rho\)

0.447

\(\mu\)

0.284

LJ16-6

T

0.988

1.020

1.052

1.084

1.116

1.148

1.180

1.212

1.244

1.252

1.272

1.292

1.312

1.332

\(\rho\)

0.813

0.801

0.789

0.777

0.764

0.748

0.733

0.717

0.702

0.695

0.684

0.673

0.662

0.650

\(\mu\)

0.051

0.056

0.060

0.065

0.071

0.077

0.084

0.090

0.098

0.101

0.107

0.111

0.116

0.122

T

1.373

1.393

1.413

1.428

1.444

1.460

1.476

1.492

1.508

1.525

1.541

\(\rho\)

0.624

0.610

0.595

0.584

0.570

0.556

0.540

0.522

0.501

0.475

0.437

\(\mu\)

0.136

0.142

0.149

0.156

0.163

0.171

0.181

0.194

0.208

0.224

0.255

Ethane

T

305

300

290

280

270

260

250

240

230

220

210

200

190

180

\(\mu\)

109

100

83.9

71.7

62.7

56.6

51.5

46.5

41.6

37.7

34.3

30.5

27.3

24.1

\({\tilde{\mu }}\)

0.324

0.297

0.250

0.213

0.186

0.168

0.153

0.138

0.124

0.112

0.102

0.091

0.081

0.072

T

160

151

141

132

120

110

100

\(\mu\)

17.9

15.4

12.6

10.1

7.27

5.2

3.37

\({\tilde{\mu }}\)

0.053

0.046

0.037

0.030

0.022

0.015

0.010