Step 1: Understanding the Process of Catalytic Reforming.
Catalytic reforming primarily involves several reactions, including dehydrogenation, isomerization, and cyclization. The process aims to break down the linear paraffin chains into branched chains or cyclic compounds, which have higher octane ratings. However, there are undesirable side reactions that can occur in this process, one of the most significant being hydrocracking.
Step 2: Analyzing the Options.
- (A) Hydrocracking of paraffins: Hydrocracking is an undesirable reaction in catalytic reforming because it breaks down the larger paraffin molecules into smaller, less valuable hydrocarbons. This reaction leads to a decrease in the yield of high-octane products. Hydrocracking is a secondary process in refining that is typically used in a separate unit to crack heavier oils into lighter products. In catalytic reforming, this is not the desired reaction, as it lowers the overall efficiency of the process.
- (B) Dehydrogenation of naphthenes: Dehydrogenation is one of the key reactions in catalytic reforming, where naphthenes (cycloalkanes) are converted into aromatic hydrocarbons by removing hydrogen atoms. This reaction is essential in improving the octane rating of the fuel.
- (C) Isomerization of naphthenes: Isomerization involves rearranging the molecular structure of alkanes to form branched-chain hydrocarbons, which also helps to increase the octane rating of the fuel. This reaction is also a desired part of the reforming process.
- (D) Cyclization of paraffins: Cyclization involves converting straight-chain hydrocarbons (paraffins) into cyclic structures, often leading to higher-octane products. This is another desirable reaction in catalytic reforming.
Step 3: Conclusion.
Since hydrocracking reduces the value of the product by breaking down larger hydrocarbons into smaller, less valuable ones, it is considered the undesirable reaction in catalytic reforming. Therefore, the correct answer is (A) Hydrocracking of paraffins.
Final Answer: Hydrocracking of paraffins
An ideal monoatomic gas is contained inside a cylinder-piston assembly connected to a Hookean spring as shown in the figure. The piston is frictionless and massless. The spring constant is 10 kN/m. At the initial equilibrium state (shown in the figure), the spring is unstretched. The gas is expanded reversibly by adding 362.5 J of heat. At the final equilibrium state, the piston presses against the stoppers. Neglecting the heat loss to the surroundings, the final equilibrium temperature of the gas is __________ K (rounded off to the nearest integer).
The residence-time distribution (RTD) function of a reactor (in min$^{-1}$) is 
The mean residence time of the reactor is __________ min (rounded off to 2 decimal places).}
Ideal nonreacting gases A and B are contained inside a perfectly insulated chamber, separated by a thin partition, as shown in the figure. The partition is removed, and the two gases mix till final equilibrium is reached. The change in total entropy for the process is _________J/K (rounded off to 1 decimal place).
Given: Universal gas constant \( R = 8.314 \) J/(mol K), \( T_A = T_B = 273 \) K, \( P_A = P_B = 1 \) atm, \( V_B = 22.4 \) L, \( V_A = 3V_B \).
The following data is given for a ternary \(ABC\) gas mixture at 12 MPa and 308 K:
\(y_i\): mole fraction of component \(i\) in the gas mixture
\(\hat{\phi}_i\): fugacity coefficient of component \(i\) in the gas mixture at 12 MPa and 308 K
The fugacity of the gas mixture is __________ MPa (rounded off to 3 decimal places).