C2.2 oil refining Flashcards
(49 cards)
Why use a hydroskimming refinery?
used for contamined HC with H2 –> pure HC + off gas
Produces H2S, NH3, H2O…
What are the 3 steps of the hydroskimming refinery (after desalting the crude oils)?
- atmospheric crude distillation
- hydrotreatment
- Catalyze reforming
Explain what the hydrotreatment step is in a hydrocracking refinery
remove heteroatoms (O,N,S) by producing H2O, H2S, NH3
conversion using H2, reduces double bond –> single bond
equilibrium, exo, heterogeneous, catalytic reaction
protect the catalyst used in downstream process
Explain the atmospheric crude distillation in a hydroskimming refinery (step1), what is the maximum T
T max = 620K or else thermal cracking and degradation of HC = coke
Seperation by boiling points
What type of reactor is used for hydrotreatment and why?
Adiabatique PBR, because T rises in reactor
What are the process conditions in hydrotreatment?
excess H2 will shift towards products
high T, high P
Explain what the catalyze reforming purpose is in a hydrockraking refinery?
^ON of gasoline
rearrengement of HC structure + aromatics
major source of H2
What is the product of hydroskimming refinery?
fuel for cars
What are 3 different types of reforming that can be used in hydroskimming?
- isomerization
- cyclisation
- aromatization
what catalyst can be used in catalyze reforming
Pt, Al2O3
*Sulfur deactivates Pt = needs hydrotreating
Why do we need multiple PBR w/ intermediate cooling, what are the 2 different options?
Because the undesired reactions will occur if T too high
quench reactors or heat exchanger reactors (x3)
For a cat rxn in adiab PBR, with increasing T:
which reactor to chose for irrev + endo
PBR with intermediate cooling
if V cte, X smaller –> need increasing V
For a cat rxn in adiab PBR, with increasing T:
Reversible + endothermic
Design with highest T as possible
For a cat rxn in adiab PBR, with increasing T:
Irreversible + exo
3-4 reactors
X is higher with more reactors
If V cte steps get smaller
For a cat rxn in adiab PBR, with increasing T:
reversible + exo
Want a lower T
kinetics will push for higher T
What is the optimal T profile for a cat + exo in PBR+ adiab?
rxn to max rate
smaller reactor V = less cat = less $ spent
exo rxn = lower T favoured
What are the 3 main steps of a cracking refinery?
- Vacuum distillation
- Catlytic cracking
- hydro-cracking
What is the difference with a cracking refinery?
extra vacuum distillation + catalytical cracking
Explain the vacuum fractionator/distillation, how does it work?
Low P = lower T boiling = limits coke formation = allows high-boiling-point fractions to be distilled without thermal cracking
used to separate heavier hydrocarbons
what happens in the disengagement zones of a vacuum fractionator?
it enhences seperation
Why use downcomers in vacuum fractionator?
controls liquid flow, pressure, efficicency…
What is a problem in vacum fractionators?
high vapor loads
What is a high vapor load, what is the impact
velocity of vapour ^= flooding = lowers engagement zones = lowers efficicency of distillation
What is the formula to describe vapor loads
Q_v = V_v * A