Modeling and Simulation of Reaction and Fractionation Systems for the Industrial Residue Hydrotreating Process



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processes-08-00032 (1)

Figure 3. The reaction network of nitrogen lumps adopted in the HCR model [24]. (HDN: 

hydrodenitrogenation). Reproduced with permission from copyright American Chemical Society

[2011]. 


According to the LHHW theory, reversible and irreversible reactions can be expressed by 

Equations (1) and (2). 

2

2

(



(

) /


)

=

m

i

i

H

H

j

j

r

whole

ADS C ADS

P

eq ADS C

R R

w

ADS

 



(1) 

2

2



(

)

=



m

i

i

H

H

ir

whole

ADS C ADS

P

R

R

w

ADS

 

(2) 



where 

r

R

  is the reversible reaction rate and 



ir

R

  is the irreversible reaction rate; 



whole

R

  is the whole 

reaction rate; 

w

  represents the inherent rate constant ascertained by basic study



i

ADS

 

and 



j

ADS

 

indicate the adsorption coefficients of lumps 



i

 and  , respectively; lump 



i

 and hydrogen 

2

H

 

are reactants; lump   is the resultant



i

C

  and 


j

C

 are the concentration of lumps 



i

 and  

respectively; 

2

H



P

  is the partial pressure of hydrogen; 



m

  is the reaction order of hydrogen



eq

 is 


the equilibrium constant of the reaction; and 

A D S

  indicates the whole LHHW adsorption coefficient, 

which expresses the competitive adsorption with diverse restrainers.   

3.2. Kinetic Model of the Asphaltene Hydrogenation Process 

The hydrogenation of resin and asphaltene with the high boiling point, and density also involves 

involute and heterogeneous catalytic reactions. Hence, by virtue of the complexity of high boiling 

point petroleum and its main products, a simple lump strategy is employed [26]. For simplification, 

resin and asphaltene are together regarded as the asphaltene lump. In the hydrogenation, three phase 

products are decomposed from asphaltene. The liquid mixtures are grouped into three lumps: the 

light oil (initial boiling point (IBP) < 350 °C) lump, the middle oil (350−540 °C) lump, and the heavy 

oil (>540 °C) lump. Gaseous gas and solid coke were taken as the gas lump and coke lump, 

respectively. Also, it is notable that the active hydrogen reaction is not considered in this paper since 


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