diff --git a/README.md b/README.md
index 766aa1b..6a349fa 100644
--- a/README.md
+++ b/README.md
@@ -147,7 +147,7 @@ Modeling and simulation of proton-exchange membrane fuel cells (PEMFC) may work
- * For more information about this model visit here
+ * For more information about this model visit here
#### 2. Larminie-Dicks Static Model
@@ -212,554 +212,551 @@ Modeling and simulation of proton-exchange membrane fuel cells (PEMFC) may work
-- |
- * For more information about this model visit here
+ * For more information about this model visit here
- #### 3. Chamberline-Kim Static Model
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- Open circuit voltage |
- V |
-
-
- b |
- Tafel's parameter for the oxygen reduction |
- V |
-
-
- R |
- Resistance |
- ohm.cm^2 |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
- A |
- Active area |
- cm^2 |
-
-
- m |
- Diffusion's parameters |
- V |
-
-
- n |
- Diffusion's parameters |
- (A^-1)(cm^2) |
-
-
- N |
- Number of single cells |
- -- |
-
-
-
- * For more information about this model visit here
- #### 4. Padulles Dynamic Model I
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- No load voltage |
- V |
-
-
- T |
- Fuel cell temperature |
- K |
-
-
- KH2 |
- Hydrogen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KO2 |
- Oxygen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- tH2 |
- Hydrogen time constant |
- s |
-
-
- tO2 |
- Oxygen time constant |
- s |
-
-
- B |
- Activation voltage constant |
- V |
-
-
- C |
- Activation constant parameter |
- A^(-1) |
-
-
- Rint |
- Fuel cell internal resistance |
- ohm |
-
-
- rho |
- Hydrogen-Oxygen flow ratio |
- -- |
-
-
- qH2 |
- Molar flow of hydrogen |
- kmol/s |
-
-
- N0 |
- Number of cells |
- -- |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
-
-
- * For more information about this model visit here
+#### 3. Chamberline-Kim Static Model
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ Open circuit voltage |
+ V |
+
+
+ b |
+ Tafel's parameter for the oxygen reduction |
+ V |
+
+
+ R |
+ Resistance |
+ ohm.cm^2 |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ A |
+ Active area |
+ cm^2 |
+
+
+ m |
+ Diffusion's parameters |
+ V |
+
+
+ n |
+ Diffusion's parameters |
+ (A^-1)(cm^2) |
+
+
+ N |
+ Number of single cells |
+ -- |
+
+
+ * For more information about this model visit here
- #### 5. Padulles Dynamic Model II
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- No load voltage |
- V |
-
-
- T |
- Fuel cell temperature |
- K |
-
-
- KH2 |
- Hydrogen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KH2O |
- Water valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KO2 |
- Oxygen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- tH2 |
- Hydrogen time constant |
- s |
-
-
- tH2O |
- Water time constant |
- s |
-
-
- tO2 |
- Oxygen time constant |
- s |
-
-
- B |
- Activation voltage constant |
- V |
-
-
- C |
- Activation constant parameter |
- A^(-1) |
-
-
- Rint |
- Fuel cell internal resistance |
- ohm |
-
-
- rho |
- Hydrogen-Oxygen flow ratio |
- -- |
-
-
- qH2 |
- Molar flow of hydrogen |
- kmol/s |
-
-
- N0 |
- Number of cells |
- -- |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
-
-
- * For more information about this model visit here
- #### 6. Padulles-Hauer Dynamic Model
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- No load voltage |
- V |
-
-
- T |
- Fuel cell temperature |
- K |
-
-
- KH2 |
- Hydrogen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KH2O |
- Water valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KO2 |
- Oxygen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- tH2 |
- Hydrogen time constant |
- s |
-
-
- tH2O |
- Water time constant |
- s |
-
-
- tO2 |
- Oxygen time constant |
- s |
-
-
- t1 |
- Reformer time constant |
- s |
-
-
- t2 |
- Reformer time constant |
- s |
-
-
- B |
- Activation voltage constant |
- V |
-
-
- C |
- Activation constant parameter |
- A^(-1) |
-
-
- CV |
- Conversion factor |
- -- |
-
-
- Rint |
- Fuel cell internal resistance |
- ohm |
-
-
- rho |
- Hydrogen-Oxygen flow ratio |
- -- |
-
-
- qMethanol |
- Molar flow of methanol |
- kmol/s |
-
-
- N0 |
- Number of cells |
- -- |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
-
-
- * For more information about this model visit here
- #### 7. Padulles-Amphlett Dynamic Model
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- No load voltage |
- V |
-
-
- T |
- Fuel cell temperature |
- K |
-
-
- KH2 |
- Hydrogen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KH2O |
- Water valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KO2 |
- Oxygen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- tH2 |
- Hydrogen time constant |
- s |
-
-
- tH2O |
- Water time constant |
- s |
-
-
- tO2 |
- Oxygen time constant |
- s |
-
-
- t1 |
- Reformer time constant |
- s |
-
-
- t2 |
- Reformer time constant |
- s |
-
-
- A |
- Active area |
- cm^2 |
-
-
- l |
- Membrane thickness |
- cm |
-
-
- lambda |
- An adjustable parameter with a min value of 14 and max value of 23 |
- -- |
-
-
- R(*Optional) |
- R-Electronic |
- ohm |
-
-
- JMax |
- Maximum current density |
- A/(cm^2) |
-
-
- CV |
- Conversion factor |
- -- |
-
-
- rho |
- Hydrogen-Oxygen flow ratio |
- -- |
-
-
- qMethanol |
- Molar flow of methanol |
- kmol/s |
-
-
- N0 |
- Number of cells |
- -- |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
- * For more information about this model visit here
- #### 8. Chakraborty Dynamic Model
-
-
- Input |
- Description |
- Unit |
-
-
- E0 |
- No load voltage |
- V |
-
-
- T |
- Cell operation temperature |
- K |
-
-
- KH2 |
- Hydrogen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KH2O |
- Water valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- KO2 |
- Oxygen valve constant |
- kmol.s^(-1).atm^(-1) |
-
-
- rho |
- Hydrogen-Oxygen flow ratio |
- -- |
-
-
- Rint |
- Fuel cell internal resistance |
- ohm |
-
-
- N0 |
- Number of cells |
- -- |
-
-
- u |
- Fuel utilization ratio |
- -- |
-
-
- i-start |
- Cell operating current start point |
- A |
-
-
- i-step |
- Cell operating current step |
- A |
-
-
- i-stop |
- Cell operating current end point |
- A |
-
-
- * For more information about this model visit here
+#### 4. Padulles Dynamic Model I
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ No load voltage |
+ V |
+
+
+ T |
+ Fuel cell temperature |
+ K |
+
+
+ KH2 |
+ Hydrogen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KO2 |
+ Oxygen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ tH2 |
+ Hydrogen time constant |
+ s |
+
+
+ tO2 |
+ Oxygen time constant |
+ s |
+
+
+ B |
+ Activation voltage constant |
+ V |
+
+
+ C |
+ Activation constant parameter |
+ A^(-1) |
+
+
+ Rint |
+ Fuel cell internal resistance |
+ ohm |
+
+
+ rho |
+ Hydrogen-Oxygen flow ratio |
+ -- |
+
+
+ qH2 |
+ Molar flow of hydrogen |
+ kmol/s |
+
+
+ N0 |
+ Number of cells |
+ -- |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ * For more information about this model visit here
+
+#### 5. Padulles Dynamic Model II
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ No load voltage |
+ V |
+
+
+ T |
+ Fuel cell temperature |
+ K |
+
+
+ KH2 |
+ Hydrogen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KH2O |
+ Water valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KO2 |
+ Oxygen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ tH2 |
+ Hydrogen time constant |
+ s |
+
+
+ tH2O |
+ Water time constant |
+ s |
+
+
+ tO2 |
+ Oxygen time constant |
+ s |
+
+
+ B |
+ Activation voltage constant |
+ V |
+
+
+ C |
+ Activation constant parameter |
+ A^(-1) |
+
+
+ Rint |
+ Fuel cell internal resistance |
+ ohm |
+
+
+ rho |
+ Hydrogen-Oxygen flow ratio |
+ -- |
+
+
+ qH2 |
+ Molar flow of hydrogen |
+ kmol/s |
+
+
+ N0 |
+ Number of cells |
+ -- |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ * For more information about this model visit here
+
+#### 6. Padulles-Hauer Dynamic Model
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ No load voltage |
+ V |
+
+
+ T |
+ Fuel cell temperature |
+ K |
+
+
+ KH2 |
+ Hydrogen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KH2O |
+ Water valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KO2 |
+ Oxygen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ tH2 |
+ Hydrogen time constant |
+ s |
+
+
+ tH2O |
+ Water time constant |
+ s |
+
+
+ tO2 |
+ Oxygen time constant |
+ s |
+
+
+ t1 |
+ Reformer time constant |
+ s |
+
+
+ t2 |
+ Reformer time constant |
+ s |
+
+
+ B |
+ Activation voltage constant |
+ V |
+
+
+ C |
+ Activation constant parameter |
+ A^(-1) |
+
+
+ CV |
+ Conversion factor |
+ -- |
+
+
+ Rint |
+ Fuel cell internal resistance |
+ ohm |
+
+
+ rho |
+ Hydrogen-Oxygen flow ratio |
+ -- |
+
+
+ qMethanol |
+ Molar flow of methanol |
+ kmol/s |
+
+
+ N0 |
+ Number of cells |
+ -- |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ * For more information about this model visit here
+
+#### 7. Padulles-Amphlett Dynamic Model
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ No load voltage |
+ V |
+
+
+ T |
+ Fuel cell temperature |
+ K |
+
+
+ KH2 |
+ Hydrogen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KH2O |
+ Water valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KO2 |
+ Oxygen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ tH2 |
+ Hydrogen time constant |
+ s |
+
+
+ tH2O |
+ Water time constant |
+ s |
+
+
+ tO2 |
+ Oxygen time constant |
+ s |
+
+
+ t1 |
+ Reformer time constant |
+ s |
+
+
+ t2 |
+ Reformer time constant |
+ s |
+
+
+ A |
+ Active area |
+ cm^2 |
+
+
+ l |
+ Membrane thickness |
+ cm |
+
+
+ lambda |
+ An adjustable parameter with a min value of 14 and max value of 23 |
+ -- |
+
+
+ R(*Optional) |
+ R-Electronic |
+ ohm |
+
+
+ JMax |
+ Maximum current density |
+ A/(cm^2) |
+
+
+ CV |
+ Conversion factor |
+ -- |
+
+
+ rho |
+ Hydrogen-Oxygen flow ratio |
+ -- |
+
+
+ qMethanol |
+ Molar flow of methanol |
+ kmol/s |
+
+
+ N0 |
+ Number of cells |
+ -- |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ * For more information about this model visit here
+
+#### 8. Chakraborty Dynamic Model
+
+
+ Input |
+ Description |
+ Unit |
+
+
+ E0 |
+ No load voltage |
+ V |
+
+
+ T |
+ Cell operation temperature |
+ K |
+
+
+ KH2 |
+ Hydrogen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KH2O |
+ Water valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ KO2 |
+ Oxygen valve constant |
+ kmol.s^(-1).atm^(-1) |
+
+
+ rho |
+ Hydrogen-Oxygen flow ratio |
+ -- |
+
+
+ Rint |
+ Fuel cell internal resistance |
+ ohm |
+
+
+ N0 |
+ Number of cells |
+ -- |
+
+
+ u |
+ Fuel utilization ratio |
+ -- |
+
+
+ i-start |
+ Cell operating current start point |
+ A |
+
+
+ i-step |
+ Cell operating current step |
+ A |
+
+
+ i-stop |
+ Cell operating current end point |
+ A |
+
+
+ * For more information about this model visit here
- Find your reports in `Model_Name` folder
- #### Screen Record
+#### Screen Record