SCES2324 Introduction to Aromatic Compounds-Student
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Transcript of SCES2324 Introduction to Aromatic Compounds-Student
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Aromatic Hydrocarbons
Benzene, Toluene and Xylene
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Physical properties
Productions of aromatic compounds
i. Physical processes: solvent extraction, azeotropic/extractive distillation, fractional distillation, solid adsorption and crystalization
ii. Chemical treatments: dehydrogenation, dehydroisomerization, and dehydrocyclization (and hydrodesulphurisation)
Reactions of aromatic compounds – alkylation, halogenation, oxidation, nitration, sulfonation etc.
Overview
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Benzene, Toluene and Xylene
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History Background
Earlier – solvent mixture
1850 – as an individual compound
Mostly side product from coal carbonization to produce coke
The yield is rather small portion
Demand for WWI – production of TNT
Because of limited production from coal carbonization, other methods have been used – catalytic reforming, pyrolysis etc
During WWII – increase demand for benzene
7.7 million tonnes per annum – US capacity
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Benzene, toluene and xylene from coal carbonization
Hydrocarbon Kg / tonne coal carbonized
Benzene 2 -8
Toluene 0.5 – 2
Xylene 0.1 – 0.5
Properties
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IUPAC name: Benzene
Other names: Benzol, Cyclohexa-1,3,5-triene
Molecular formula: C6H6
Molar mass: 78.1121 g/mol
Appearance: Colorless liquid
Density: 0.8786 g/cm3, liquid
Melting point: 5.5 oC
Boiling point: 80.1 oC
Solubility in water: 1.79 g/L (25 oC)
Viscosity: 0.652 cP (20 oC)
Dipole moment: O D
Main hazards: Carcinogenic, toxic
Flash point: -11 oC
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IUPAC name: Methylbenzene
Other names: Toluene, Phenylmethane, Toluol
Molecular formula: C7H8 (C6H5CH3)
Molar mass: 92.14 g/mol
Appearance: Clear colorless liquid
Density: 0.8669 g/cm3, liquid
Melting point: -93 oC
Boiling point: 110.6 oC
Solubility in water: 0.053 g/100 ml (20 - 25 oC)
Viscosity: 0.590 cP (20 oC)
Dipole moment: O.36 D
Hazards: Highly flammable
Flash point: 4 oC
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IUPAC name: 1,2-dimethylbenzene 1,3-dimethylbenzene 1,4-dimethylbenzene
Common name: o-xylene m-xylene p-xylene
Other names: o-xylol, Orthoxylene m-xylol, Metaxylene p-xylol, Paraxylene
Molecular formula:
C8H10 (C6H4C2H6)
Molar mass: 106.16 g/mol
Appearance: Clear colorless liquid
Density: 0.88 g/cm3, liquid 0.86 g/cm3, liquid 0.86 g/cm3, liquid
Melting point: -25 oC -48 oC 13 oC
Boiling point: 144 oC 139 oC 138 oC
Solubility in water: Practically insoluble
Viscosity: 0.812 (20 oC) 0.62 (20 oC) 0.34 cP (20 oC)
Dipole moment: -
Hazards: Harmful
Flash point: 17 oC 25 oC 25 oC
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Production of Aromatics
Physical Processes
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Separation of AromaticsPhysical methods
1. Fractional distillation
2. Azeotropic distillation
3. Extractive distillation
4. Solvent extraction
5. Solid adsorption
6. Crystallization
Consideration
1. Close or identical boiling points
2. Reversible condition under reforming reactions
3. Solubility and miscibility
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Fractional Distillation
Separate toluene
Benzene forms azeotropic mixture with naphthenes and paraffins
Products from catalytic reforming process is separated light fraction – boiling point at 180 – 250 oC
Further separation at above 225 oC to produce 90% toluene and 10% azeotropic mixture of benzene, naphthenes and paraffin
Aromatics separation plants:
Reformate moves up
Solvent moves down
Solvent extracted out to a stripper
Separate from alkanes and cycloalkanes
Further separation by fractional distillation
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Aromatics Separation Plant
?
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Separation of C8 Aromaticso-xylene separate by fractional distillation
Not possible for m- and p-xylene (preferred methods is crystallization or isomerization)
C8 stream
distillation
Crystallization or adsorption
p-xylene
o-xylene
Residual C8s
C8 stream
p-xylene separation
p-xylene
o-xylene
Isomerisation
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The process requires specific solvent or azeotropic agent
As a volatile component in the mixture
Increase the rate of volatility – change the properties and encounter the separation problem
Example: separation of toluene
Azeotropic agents:
1.
2.
3.
4.
Increase the volatility of toluene
Distill off from benzene and xylene
See FIG. 3. and TABLE 3
Azeotropic D
istillation
?
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In the presence of a solvent that reduced the volatility rate of the compounds to be separated
Lower the boiling point of the component
The added solvent must fit the properties:
1.
2.
3.
4.
5.
6.
See FIG. 4
Extractive Distillation
?
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Examples:
Requires additional process for purification
1.Benzene treated with sulphuric acid; washed with caustic soda, water; separate polymers and sulphonate sludges in the re-run tower
2.Toluene treated with maleic anhydride, caustic soda, water; dried under calcium chloride
compound solvent
Xylene cresol
Benzene and toluene phenol
Extractive Distillation
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Solvent has highly selectivity for aromatics against non-aromatics
Fit the following characters:
1.Form two phase system, able to separate at reasonable range of temperature
2.Non-corrosive
3.Non-reactive to the feed and the product
4.Thermally stable
Examples:
Udex Plant – aqueous diethylene glycol
Refinery of Humble Oil – SO2 extraction-double solvent extraction
Solvent Extraction
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UDEX Plant
Separate benzene, toluene and xylene in a plant
Main component: an extractor, a water wash, a heater, a contact clay treater and distillation columns
Diethylene glycol-water increase the selectivity
More water will decrease the solubility
See FIG. 5, TABLE 4
Solvent Extraction
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SO2 Extraction-Double Solvent Extraction
Toluene separation
First extraction: separate aromatics from non-aromatics by adding SO2
Second extraction: oil wash, then separate raffinate (SO2, oil wash and some non-aromatics) by extraction
SO2 and oil wash are reused
After removal of SO2 and oil wash to obtain 99.5% toluene
After acid wash to obtain 100% toluene
See FIG. 6
Solvent Extraction
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Adsorption of organic compounds on compressed silica gel
Aromatics prefer to adsorb
Washing silica gel with xylene to remove aromatics from non-aromatics
The silica gel can be reused by washing with a paraffin solvent
Commercially known as Arosorb process
Aromatics and non-aromatics
xylenes
Xylenes + aromatics
Washing with paraffin
Solid Adsorption
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Boiling points of isomers of xylene are very close each other:
Ethylbenzene: 136.2 oC
p-xylene: 138.2 oC
m-xylene: 139.1 oC
o-xylene: 144.4 oC
Separation by fractional distillation is impossible
Freezing temperatures of isomers of xylene
Ethylbenzene: -95.0 oC
p-xylene: 13.3 oC
m-xylene: -47.9 oC
o-xylene: -25.2 oC
Process: dried over activated alumina, cooled in two stages (first crystallisation of p-xylene at 13.3 oC in ‘waiting tank’, centrifuge, second crystallization)
Product: 95%, with 60-70% recovery
Crystallization
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Production of Aromatics
Chemical Processes
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An Overview1. Catalytic reforming
2. Dehydrogenation
3. Dehydroisomerisation
4. Pyrolysis Gasoline
5. Isomerisation
6. Hydrodealkylation
7. Disproportionation
8. Desulfuration
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Also known as ‘hydrogen reforming’
Purposely to obtain main aromatic compounds (benzene, toluene, and xylenes) as much as possible
Three main types:
Dehydrogenation of cyclohexane and homologues
Dehydroisomerisation of methyl cyclopentane and homologues
Dehydrocyclisation of alkanes
Other related processes
Pyrolysis gasoline
Hydrodealkylation
Isomerisation
Desulfuration
Catalytic Reform
ing
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Mostly the feedstocks are from naphthenes and homologues
‘Hydroforming’ process
Condition: ~500 oC, ~15 atm, dehydrogenation catalyst, a flow of hydrogen gas
Catalysts: molybdenum oxide, chromic oxide, Pt, Cu (mono-function catalyst)
Fisher and Welty
Feedstock: methyl cyclohexane,
Product: toluene
See attachment FIG. 1: Hydroformer
Dehydrogenation?
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Combination of isomerisation and dehydrogenation processes
Mostly from substituted cyclopentanes
Examples: methyl cyclopentane, dimethyl cyclopentane etc.
Condition: ~500 oC, ~15 atm, hydrogen atmosphere
Catalyst: molybdenum oxide, chromic oxide, Pt, Cu
Dehydroisom
erisation
?
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Hartley
Feedstock: mixture of methyl cyclopentane and cyclohexane
Product: benzene
Reason: the rate of isomerisation is slower than dehydrogenation, so that cyclohexane form benzene very quickly
Feedstock: dimethyl cyclopentanes, ethyl cyclopentane
Primary product: methyl cyclohexane (isomerisation)
Secondary product: toluene (dehydrogenation)
Dehydroisom
erisation
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Greensfelder and Fuller
Feedstock: methyl cyclopentane
Condition: 490 oC, 10 – 20 atm, a flow of hydrogen
Catalyst: MoO3 on activated alumina
Product: benzene (no cyclohexane)
Platforming
Feedstocks: straight run gasoline containing methyl cyclopentane, cyclohexane, and other C6 and C8 naphthenes
Condition: 475 oC, hydrogen atmosphere, 720 psi
Catalyst: Pt on alumina
Reactor: pellitized Pt working at 250 – 275 oC
Product: mixture of benzene and other aromatics
See attachment: FIG. 2: Platformer
Dehydroisom
erisation
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Fulton
Feedstocks: mixture of paraffins (13.4 %), isoparaffins (29.3 %), naphthenes (33.3 %), aromatics (6.1 %)
Condition: platforming
Product: 60 % isoparaffins and 40 % aromatics
Haensel and Berger
Feedstocks: mixture of C7 – C8 paraffins (28 %), C7 – C8 naphthenes (62 %), toluene (10 %)
Condition: platforming
Product: 53 - 56 % toluene
Edgar
Feedstock: naphthenes
Condition: 480 – 510 oC, 14 – 21 atm
Catalyst: Pt on alumina, and halides
Yield: 90 % aromatics HC
Dehydroisom
erisation
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Advantages of the platforming process:
1. The naphthenes converted to aromatics
2. Isomerisation and cracking of the paraffins to improve the octane rating
3. The sulfur content is decreased
Caterole process
Introduce in England
Hydrocarbon stream heated at 600 - 700 oC with slightly above atmospheric pressure
Catalyst: copper or copper-iron
An example of the process
Feedstock: naphtha fraction (120 – 240 oC)
Condition: 700 oC, 20 – 50 psi, straight distillation
Product: benzene (92 – 94 %)
from another fraction to obtain toluene (94 – 96 %)
Can also produce xylenes, ethylbenzene, styrene, indene, naphthalenes, antracene etc
Dehydroisom
erisation
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Ring closure of alkanes (paraffins)
Usually C6 or more
Proceed via olefins
A slower reaction than the dehydrogenation and dehydroisomerisation
Involve transformation of paraffins to olefins, ring closure to form naphthenes, and dehydrogenation
Condition: >500 oC
Therefore, inclusive reaction of cracking of alkanes
Dehydrocyclization
?
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Hoog, Verheus and Zuiderweg
Feedstock: olefins
Condition: 450 – 550 oC
Catalyst: Chromic oxide, or other metal oxides and sulfides
Product: aromatics
Examples of paraffins conversion at 465 oC:
Paraffin hydrocarbon Aromatic hydrocarbon % aromatization
n-Hexane Benzene 19.5
2-Methylhexane Toluene 31
n-Heptane Toluene 36
2,5-Dimethylhexane Mostly p-xylene 52
3-Methylheptane Mainly o- and p-xylene 35
n-Octane Mainly o-xylene 46
n-Nonane Mainly methylethylbenzene 58
Dehydroisom
erisation
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Shell Development Company
Feedstock: n-heptane
Condition: 490 oC, atmospheric pressure
Catalyst: 10 % Chromic oxide on alumina, cerium dioxide and potassium oxide
Product: toluene (80 % conversion), usually maintained at 40 %
Feedstock: n-nonane
Condition: 465 oC, atmospheric pressure
Catalyst: 70 % chromic oxide, 30 % alumina with potassium oxide
Product: 71 % aromatics, 6% olefins, 23 % paraffins
Aromatics was 80 % methylethylbenzene
Dehydroisom
erisation
?
?
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Hurley
Feedstock: heptane (90 %), air (5%), HF (5 %)
Condition: 550 oC, atmospheric pressure,
Catalyst: ferric fluoride and manganous fluoride
Product: toluene (42 %)
Dunstand, Haque, Wheeler
Feedstock: C2 to C6 paraffins
Condition: 750 – 900 oC
Product: benzene (and other liquid aromatic products)
Dehydroisom
erisation
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Frey and Hepp
Suggest the mechanism of the aromatization from ethane feedstock
Two steps; dehydrogenation (endothermic), aromatization (exothermic)
When the process through ethylene and butadiene
Dehydroisom
erisation
?
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A fraction from cracking process with a boiling range between 20 – 200 oC
The stream contains aromatics, alkenes, dienes, alkanes and cycloalkanes
Most of the alkenes and dienes were removed by solvent extraction
Condition: 75 – 150 oC, 10 – 40 atm, fraction distillation
Product: C6 – C8 hydrocarbons, benzene, toluene, C8 aromatics
Typical products distribution (%):
Reformate Pyrolysis gasoline
Benzene 11 54
Toluene 55 31
C8 aromatics 34 15
Pyrolysis Gasoline
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Involve 1,2-hydride or methyl shifts
A stage to produce more o- and p-xylenes
Feedstock: C8 aromatics
Condition: vapour phase, 500 oC, strong acidic condition
Catalyst: silica-alumina
Product: o-xylene (20 %), m-xylene (55 %), p-xylene (25 %)
Ethylbenzene not isomerised to xylenes unless the presence of catalytic reforming process
Isomerisation?
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In term of market demand, benzene is higher than toluene
But toluene produced in excess
Transforms toluene to benzene
Feedstock: toluene
Catalytic condition: 550 – 650 oC, 35 – 70 atm
Non-catalytic condition: 650 – 750 oC, 20 – 67 atm
Yield: up to 99 %
Market From petroleum From coal tar
Benzene 65 10 80
Toluene 20 40 15
Xylenes 15 50 5
Hydrodealkylation
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Converted toluene to benzene and o-, m-, and p-xylenesCondition: 480 oCCatalyst: zeolite (acidic catalyst)
Disproportionation
A process to avoid ‘poisoning’ to catalyst
Sulphurated compounds removed by this process
The feedstock pre-treated with cobalt oxide or molybdenum oxide at 400 oC
Sulphurated compounds turn into H2S – easier to remove
Desulfuration