Catalytic reforming: evaluate the primary effect of increasing operating pressure in the reforming reactor, considering its influence on coke formation tendency, intrinsic reaction rates/selectivity, and the octane number of the produced gasoline (reformate).

Difficulty: Medium

Correct Answer: None of these

Explanation:


Introduction / Context:
Catalytic reforming (platforming) converts low-octane naphtha into high-octane reformate by dehydrogenation of naphthenes to aromatics, isomerization, and limited hydrocracking. Operating variables include temperature, pressure, hydrogen partial pressure, and space velocity. This question asks what happens when reactor pressure is increased, and which of the listed statements correctly reflects industry practice and equilibrium principles.

Given Data / Assumptions:

  • Feed: hydrotreated naphtha rich in paraffins/naphthenes.
  • Key reactions: endothermic dehydrogenation to aromatics + H2; isomerization; mild hydrocracking.
  • Variable of interest: higher total/partial pressure of hydrogen.


Concept / Approach:
Dehydrogenation and aromatization produce hydrogen; by Le Chatelier's principle, raising pressure and H2 partial pressure shifts equilibria against aromatic formation. As a result, octane number (primarily from aromatics) tends to decrease at higher pressure. Higher hydrogen partial pressure also suppresses coke formation on the catalyst surface, improving run length, not worsening coking. Apparent reaction rates for the desired endothermic dehydrogenations do not increase simply by raising pressure; severity is commonly achieved with higher temperature or lower pressure/space velocity.

Step-by-Step Solution:

1) Identify desired pathway: naphthene → aromatic + H2 (endothermic, equilibrium-limited).2) Increase pressure: equilibrium shifts toward fewer moles of gas, disfavoring H2 generation and therefore aromatics formation.3) Outcome: lower aromatic yield → lower reformate octane at higher pressure.4) Coking: higher H2 partial pressure suppresses coke; so coking does not increase.5) Rate/severity: endothermic dehydrogenations are not accelerated by pressure; severity is typically raised by temperature or reduced pressure.


Verification / Alternative check:
Operating strategies in reformers favor lower pressures (within metallurgy/decoking constraints) to maximize octane and hydrogen yield, accepting higher coking propensity controlled by good hydrotreating and regeneration cycles.


Why Other Options Are Wrong:

Increases coke formation: incorrect; higher H2 suppresses coke.Increases rate/severity: not a general truth for reforming dehydrogenations.Produces higher octane: opposite of observed trend; octane typically drops as pressure rises.


Common Pitfalls:
Assuming that higher pressure always accelerates reactions or improves quality; for equilibrium-limited dehydrogenations, lower pressure is favorable to octane.


Final Answer:
None of these

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