Skip to main content

Table 2 The values of f ′′ (0), − θ ′ (0), and θ (0) for various values A ∗ , B ∗ , S , N , γ , E c , and β

From: Thermal analysis of conducting dusty fluid flow in a porous medium over a stretching cylinder in the presence of non-uniform source/sink

A ∗

B ∗

P r

Q

β

γ

S

−f"(0)

−θ′(0)

θ(0)

0.2

0.2

3.0

1.0

0.1

0.5

0.5

1.82157

1.81112

0.764171

0.4

      

1.82157

1.74642

0.7829819

0.6

      

1.82157

1.68173

0.801791

0.2

0.2

3.0

1.0

0.1

0.5

0.5

1.82157

1.81112

0.764171

 

0.4

     

1.82157

1.75226

0.778672

 

0.6

     

1.82157

1.69122

0.794108

0.2

0.2

3.0

1.0

0.1

0.5

0.5

1.82157

1.81112

0.764171

  

5.0

    

1.82157

2.29439

0.720947

  

7.0

    

1.82157

2.65646

0.705487

0.2

0.2

3.0

1.0

0.1

0.5

0.5

1.82157

1.81112

0.764171

   

1.5

   

1.97352

1.81919

0.757088

   

2.0

   

2.11317

1.82094

0.752149

0.2

0.2

3.0

1.0

0.0

0.5

0.5

1.80043

0.8622

1.041606

    

0.05

  

1.81322

1.40414

0.880658

    

0.1

  

1.82157

1.81112

0.764171

0.2

0.2

3.0

1.0

0.1

0.0

0.5

1.60946

1.61563

0.823394

     

0.2

 

1.69472

1.66004

0.806224

     

0.4

 

1.77971

1.7598

0.777936

     

0.6

 

-1.863

1.86194

0.750953

0.2

0.2

3.0

1.0

0.1

0.5

0.0

1.65356

1.79255

0.774557

      

0.5

1.65356

1.79255

0.774557

      

1.0

1.97352

1.81919

0.757088

      

1.5

2.11317

1.82094

0.752149