Catalytic Cracking, Hydrocracking Flashcards

1
Q

Catalytic Cracking

A

Process that breaks down the larger, heavier, and more complex hydrocarbon molecules into simpler and lighter molecules by heat and aided by catalyst

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2
Q

Feedstocks for catalytic cracking

A

atmospheric and vacuum crude unit gas oils and coker gas oil

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3
Q

How is catalyst regenerated? Describe the movement

A

Burning off coke with air. The catalyst is continuously moved from reactor to regenerator and back to reactor

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4
Q

The cracking reaction is ___

A

endothermic

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5
Q

The regeneration reaction is ___

A

Exothermic

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6
Q

What are heat balance units

A

Units that use the heat from regeneration to heat the preheat the feed going into the reaction

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7
Q

2 types of bed for catalytic cracking

A

moving-bed or fluidized bed

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8
Q

Define TCC and FCC. What are their differences

A

Themafor catalytic cracking (moving -bed) and Fluid catalytic cracker (fluidized bed).

In TCC the catalyst is moving while in FCC it is fluidized. Few TCC are left as FCC has taken over.

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9
Q

Describe main pathways in fluidized bed catalytic cracking

A

The hot oil feed makes contact with the catalyst in either the feed riser line (transfer line) or the reactor.

As the cracking reaction progresses, the catalyst is progressively deactivated by the formation of coke on the surface of the catalyst.

The catalyst and hydrocarbon vapors are separated mechanically.

The oil vapors are taken overhead to a fractionation tower for separation into streams having the desired boiling ranges.

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10
Q

What happens to the oil/hydrocarbons remaining on the spent catalyst?

A

It is removed by steam stripping before the catalyst enters the regenerator

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11
Q

What happens to the spent catalyst?

A

It flows into the regenerator and is reactivated by burning off the coke deposits with air

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12
Q

What happens to the flue gas and catalyst?

A

separated by cyclone separators and electrostatic precipitaors

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13
Q

Describe the catalyst used in FCC

A

They are very fine particles which behave as a fluid when aerated with vapor. When fluidized, they act as a vehicle to transfer heat from the regenerator to the oil feed and reactor.

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14
Q

Two types of FCC units

A

side-by-side and stacked

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15
Q

How is regenerator temp and coke burn-off controlled?

A

By varying the air flow rate

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16
Q

The heat of combustion raises the catalyst temperature from ___ to ____ . The regenerated catalyst contains ____ to ____ wt% residual coke.

A

1150 to 1550 F

0.01 to 0.4 wt%

17
Q

what is burned coke in the form of?

A

CO and CO2 or completely CO2 depending on regenerator design.

18
Q

Cracking Reaction (3)

A

Paraffin -> Paraffin + Olefin

Alkyl napthene -> Napthene + olefin

Alkyl aromatic -> aromatic + olefin

19
Q

3 classes of commercial cracking catalysts. Which are most common?

A

(1) acid-treated natural aluminosilicates
(2) amorphous synthetic silica-alumina combinations
(3) crystalline synthetic silica-alumina catalyst (zeolites or molecular sieves)

Class 3 or a mixture of 2 and 3 are most common

20
Q

Advantages of zeolite catalyst over amorphous ones. (6)

A
  1. Higher activity
  2. Higher gasoline yield at a given conversion
  3. Production of gasoline containing larger
    percentage of paraffinic and aromatic hydrocarbons
  4. Lower coke yield (= larger throughput at a given conversion level)
  5. Increased isobutene production
  6. Ability to go to higher conversions per pass without overcracking.
21
Q

Which catalyst is cheaper? Amorphous or Zeolites

22
Q

What are poison to cracking catalysts? Explain how

A

Nitrogen compounds, iron, nickel, vanadium, and copper.

Nitrogen reacts with the acid centers on the catalyst and lowers its activity.

The metals accumulate on the catalyst causing a reduction in throughput by increasing coke formation.

23
Q

(T/F) In catalysts, small pores results in lower activities

A

False (it is higher)

24
Q

Major operating variables affecting conversion and product distribution (6)

A

charge stock
cracking temperature
catalyst/oil ratio:
space velocity
catalyst type and activity
recycle ratio

25
Q

Ability:

A

Ability to crack a gas oil to lower boiling fractions.

26
Q

Catalyst/oil ratio (C/O)

A

lb catalyst/lb feed

27
Q

Conversion

A

100
(volume of feed - volume of cycle stock)/(volume of feed)

28
Q

Efficiency

A

% gasoline x conversion

29
Q

Recycle Ratio:

A

Volume recycle / volume of fresh feed

30
Q

Selectivity

A

Ratio of yield of desirable products to the yield of undesirable products

31
Q

Space velocity

A

Can be defined on either volume (LHSV) or weight (WHSV) basis

LHSV (liquid hour space velocity): (volume feed)/ (volume catalyst )(hr)

WHSV (weight hour space velocity, hr-1): (lb feed)/ (lb catalyst) (t) where t is the catalyst residence time in hr.

32
Q

What increases conversion?

A

Increase in rxn temp (up to a certain point), catalyst/oil ratio, catalyst activity, and contact time.

Decreasing space velocity

33
Q

(T/F) increase in conversion = increase in gasoline yield

34
Q

CC:
Effect of increasing pressure? What is typical pressure range

A

It increases coke yield and decreases gasoline octane.

15-20psig

35
Q

With the trend to heavier feedstocks, the carbon-forming potential of catalytic cracker feeds is increasing. What is being done to offset this?

A

Some units with limited blower capacity are adding oxygen to the air to the regenerator.

Oxygen contents of the gases to the regenerator are being increased to 24 to 30% by volume (limited by regenerator temperature capacity and heat
removal capacity.)

36
Q

What is cataly