Chapter 5a -_cracking
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Transcript of Chapter 5a -_cracking
CHAPTER 5
C R A C K I N G
CHAPTER 5 OUTLINE• Cracking• Fluid catalytic crackingI. PrinciplesII. Recent developmentsIII. FeedstockIV. Product yields and qualitiesV. Catalyst and operating parameters
• HydrocrackingI. PrinciplesII. Process requirementsIII. Product yields and qualitiesIV. Residue cracking
OIL REFINING
• Method by which crude oil convertedtopetroleum products
– (I think that a barrel (42 gal—produces 44gal of
petroleum products)• Distillation (fractionation)
– At high temperature the lightest fractions rise to the top of a tower, heavier fractions condense at bottom
OIL REFINING
Typical Oil– Gasoline C4 to C10 27%– Kerosene C11 to C13 13%– Diesel C14 to C18 12%– Heavy gas oil C19 to C25 10%– Lubricating oil C26-C40 20%– Residue >C40 18%
OIL REFINING
• Thermal Cracking
• Catalytic Cracking
OIL REFINING
• What we get out of oil now with modernrefineries:– 50% gas– 30% fuel
oil– 7.5% jet
fuelHOW??
CRACKING• Crude oil contains many large molecules. If these are to
be used as fuels or feedstock for the chemical industry then they have to be cracked into smaller molecules.
• When hydrocarbons burn they are reacting with oxygen in the air. In general, the smaller the molecule the better it will mix and then react with the air.
Fuel gas Naphtha Diesel
Petrol KerosineFuel Oil and bitumen
CRACKINGInvolves the breaking of C-C bonds in alkanes
Converts heavy fractions into higher value products
• THERMALproceeds via a free radical mechanism
• CATALYTICproceeds via a carbocation (carbonium ion) mechanism
• High Pressure ... 7000 kPa• High Temperature ... 400°C to 900°C• Free Radical Mechanism• Homolytic fission• Produces mostly alkenes ...e.g. ethene
formaking polymers and ethanol
• Produces Hydrogen ... used in theHaber Process and in margarine manufacture
• Bonds can be broken anywhere in the moleculeby C-C bond fission or C-H bond fission
THERMAL CRACKING
• Slight pressure• High Temperature• Use catalyst toCatalysts include
speed up the crackingreaction. zeolite,aluminium hydrosilicate,bauxite and silica alumina.
• Carbocation Mechanism• Heterolytic fission• Produces branched and cyclic alkanes,
naromatichydrocarbons used for motor fuels
**ZEOLITES are crystalline aluminosilicates; clay like substances
CATALYTIC CRACKING
•Catalytic cracking is similar to thermal cracking except that catalystsfacilitate the conversion of the heavier molecules into lighter products.
•Use of a catalyst (a material that assists a chemical reaction but does not take part in it) in the cracking reaction increases the yield of improved-quality products under much less severe operating conditions than in thermal cracking.
•Typical temperatures are from 450°-510° C at much lower pressures of 10-20 psi.
•The catalysts used in refinery cracking units are typically solid materials (zeolite, aluminum hydrosilicate, treated bentonite clay, fuller's earth, bauxite, and silica-alumina) that come in the form of powders, beads, pellets or shaped materials called extrudates.
CATALYTIC CRACKING
There are three basic functions in thecatalyticcracking process:
I. Reaction: Feedstock reacts with catalystandcracks into different hydrocarbons;
II. Regeneration: Catalyst is reactivatedby burning off coke; and
III. Fractionation: Cracked hydrocarbon stream isseparated into various products.
BASIC FUNCTIONS INCATALYTIC CRACKING
molecules• Large hydrocarbons are broken into smaller using heat and a catalyst.
• This process is known as catalytic cracking.• The small molecules produced are then separated by
distillation.
CATALYTIC CRACKING PROCESS
CatalyticcrackerHeat to
vaporise
Distillationtower
pressure
Big Molecules
Smal
ler m
olec
ules
Molecules break up
In the catalytic cracker long chain molecules are‘cracked’. An example of such a reaction is:
C8H18 C6H14 + C2H4
CC
H
H
H
H+
ethene
H H H H H H H HH C C C C C C C C H
H H H H H H H H
Octane
HH H H H H H C C C C C C H H H H H H
H
hexane
Ethene is used to make plastics
Heat pressure catalyst
Used as a fuel
CATALYTIC CRACKING REACTION
CATALYTIC CRACKING REACTION• Products formed are the result of both
primaryand secondary reactions.• Primary rxns – involve the initial C-C bondscission and the immediate neutralization of the carbonium ion.
• Primary rxns as below:Paraffin paraffin + olefin
Alkyl napthene napthene + olefin Alkyl aromatic aromatic + olefin
CLASSIFICATION OFCATALYTIC CRACKING
• Catalytic cracking processes can be classified as either moving-bed (Thermafor catalytic cracking - TCC) or fluidized-bed units (FCC).
• Very few TCC units in operation today, FCC unit has taken over the field – where the major fraction of the cracking reaction occurs.
PROCESS FLOW OFCATALYTIC CRACKING
• Process flows for FCC and TCC are similar.• The hot oil feed is contacted with catalyst in either the
feed riser or the reactor.• The catalyst is progressively deactivated by
theformation of coke on the surface of the catalyst.• Catalyst and hydrocarbon vapors are
separatedmechanically, oil remaining on the catalyst is removedby steam stripping before catalyst enterstheregenerator.• The oil vapors are taken overhead to afractionationtower for separation into streams having thedesired boiling ranges.
CATALYST REGENERATEDWhat happen to the catalyst then?• It flows into the regenerator and is activated by burning
off the coke deposits with air.• Regenerator temperatures are carefully controlled to
prevent catalyst deactivation by overheating and to provide the desired amount of carbon burn-off. – by manipulating the air flow in the exit flue gas.
• Flue gas & catalyst are separated by cyclone separatorsand electrostatic precipitators.
• Important to make sure the catalyst is steam-stripped as it leaves the generator, to remove the adsorbed oxygen before it is contacted with the oil feed.
FLUIDIZED –BED CATALYTIC CRACKING
Introduction - FCC
• The fluidized catalytic cracking (FCC) unit is the heart of the refinery and is where heavy low-value petroleum stream such as vacuum gas oil (VGO) is upgraded into higher value products, mainly gasoline and C3/C4 olefins, which can be used in the alkylation unit for production of gasoline (C7– C8 alkylates).
• Major developments have occurred in areas of newcatalysts and new reactor and regenerator designs.
Role of FCC in the Refinery
• The role of the FCC is to take heavy desulphurised feedstock and crack it into lighter, mainly high octane gasoline.
• The FCC also produces olefins (C5 = and C4 =) and LPG.
FCC Process Flow Diagram
Introduction - FCC
• FCC employs a catalyst in the form of very fine particles (70 microns), that can behave as a fluid when aerated with a vapor.
• Two type of FCC units:I. Side-by –side type, where the reactor and
regenerator are separate vessels adjacent to each other
II. Orthoflow/stacked type, reactor is mountedon top of the regenerator.
Zeolite as Catalyst in FCC
• Early attempts to increase production of light olefins from the FCC were based primarily on process variables.
• Poor selectivity of this approach resulted in excess production of dry gas and coke.
• By 1970s, researchers found that non-Y zeolites could also co-produce light olefins (C2= to C5=), often at the expense of gasoline.
Zeolite as Catalyst in FCC
• Thedevelopment
chronology offor
catalyst and additivesthe
lightto enhance production of olefins in FCCs.
Feedstock
• The main feedstock used in a FCC unit is the gas oil , which can be considered mixtures of aromatic, naphthanic and paraffinic molecules.
• There are also varying amounts of contaminants such as sulphur, nitrogen and metals. To protect thecatalyst, required
feed pre-treatment byhydrotreating is in order toremove contaminants(especially sulphur) and improve
cracking characteristics and yields.
• Nitrogen tends to poison the catalyst by neutralising its acid sites. However, the FCC process is unaffected if the nitrogen content level is controlled below 0.2%.
• The acidity and unique porous structures of zeolites play an important role in controlling the activity and selectivity of many zeolite-based catalysts.
• Some possible feedstocks atmospheric distillates, coking distillates, visbreaking distillates, VGO, atmospheric residue (desulphurised) and vacuum residue (desulphurised, deasphalted).
Feedstock
FCC products