Table 2 DSL parameters and heat of adsorption for activated carbon and zeolite 5 A11.

From: Optimization of pressure swing adsorption in a three-layered bed for hydrogen purification using machine learning model

 

\({k_1}\) (mmol/g)

\({k_2}\) (1/atm)

\({k_3}\) (K)

\({k_4}\) (mmol/g)

\({k_5}\) (1/atm)

\({k_6}\) (K)

\({Q_i}\) (cal/mol)

Activated carbon

H2

2.4 × 10−5

9.0 × 10−4

1700

4.8 × 10−4

6.0 × 10−5

1915

− 1800

CO

3.65 × 10−3

8.7 × 10−5

2003

4.37 × 10−4

2.0 × 10−3

2050

− 4000

CH4

5.8 × 10−3

1.0 × 10−4

2060

7.4 × 10−4

3.5 × 10−3

2200

− 5600

CO2

8.0 × 10−3

8.0 × 10−6

3100

1.4 × 10−3

9.6 × 10−7

4750

− 5900

Zeolite 5 A

H2

7.8 × 10−4

9.0 × 10−5

1647

7.0 × 10−6

1.2 × 10−5

3000

− 1500

CO

2.3 × 10−3

9.7 × 10−5

2920

9.5 × 10−4

7.9 × 10−5

3280

− 7000

CH4

2.6 × 10−3

2.1 × 10−4

2200

7.5 × 10−4

3.0 × 10−9

4800

− 4600

CO2

3.0 × 10−3

1.1 × 10−3

2508

1.4 × 10−3

1.0 × 10−2

3300

− 8500