1 CHM 585 / 490 Chapter 4. 2 Benzene / Toluene / Xylene Terephthalic Acid Cumene Phenol / Acetone / Bisphenol A.

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CHM 585 / 490

Chapter 4

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Chapter 4

• Benzene / Toluene / Xylene

• Terephthalic Acid

• Cumene

• Phenol / Acetone / Bisphenol A

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BTX

• Benzene / Toluene / Xylene

• Predominantly ( about 90%) from oil

• From reformate gasoline and pyrolysis gasoline

• BTX Content– Reformate: 3/13/18– Pyrolysis gasoline: 40/20/5

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Reformate Gasoline

• Distillation of crude oil gives low octane fractions which must be “reformed” before using as gasoline.

• The fractions are mainly branched and unbranched alkanes and cycloalkanes

• Reforming involves heating at 500ºC with acidic isomerization catalysts (e.g. Al2O3

.

SiO2) and Pt followed by distillation

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Pyrolysis gasoline

• From the cracking of naptha for the production of ethylene, propylene, and other olefins.

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Isolation of Aromatics from Reformate and Pyrolysis Gas

• Problems with fractional distillation– Cyclohexane, n-heptane, and other alkanes

form azeotropes with benzene and toluene– Minor difference between boiling points of the

C8 components. e.g.:• Ethylbenzene 136.2 ºC p-xylene 138.3 ºC

• m-xylene 139.1 ºC o-xylene 144.4 ºC

• Separation requires special processes

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Separation Techniques

• Azeotropic distillation

• Extractive distillation

• Liquid-liquid extraction

• Crystallization

• Adsorption

Let’s review azeotropes before continuing

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Fractional Distillation

• Begin at a1 and heat to T2.– a2 is the liquid composition.– a2’ is the vapor composition.– Vapor is richer in A than the

liquid.

• Cool the vapor until condenses at T3.– a3 is the liquid composition.

– a3’ is the vapor composition.– Vapor is even richer in A

• Repeat until pure A is obtained.

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Fractionating Column and Efficiency

• The number of theoretical plates is the number of effective vaporization and condensation steps required to achieve a condensation of given composition from a given distillate.

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Azeotropes

• In some real systems, the temperature / composition curve is far from ideal. A maximum or minimum in the curve is possible; this is an azeotrope.

• At the azeotrope, the liquid and vapor have the same composition

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High boiling azeotrope Low boiling azeotrope

•Makes physical separation of the two components impossible.

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Distillation of Ethanol

• Azeotrope is around 95 % ethanol..

13Impossible to distill ethanol to greater than 95%.

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Azeotropic Distillation to Isolate Aromatics

• Best when high aromatic content• The addition of strongly polar agents (amines,

alcohols, ketones, water) facilitates the removal of alkanes and cycloalkanes as lower boiling azeotropes

• For example, add acetone to remove nonaromatics from the benzene fraction and then extract the acetone from the benzene with water.

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Extractive Distillation

• An additive is used to increase the differences in boiling points

• For example, add NMP (N-methylpyrrolidone)

• This increases the boiling point of the aromatics by “complexation” of the electrons in the aromatic ring with the NMP and therefore facilitates separation

NO

CH3

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Liquid-liquid extraction

• Same principle as the separatory funnel, but continuous. Based upon countercurrent flow.

• The mixture is added to the middle of a column. The extraction liquid is added to the top. The non aromatics leave the column at the top and the aromatics with solvent exits from the lower part of the column

• Most extraction processes provide a mixing zone followed by a settling zone.  

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Crystallization

• Mainly to separate xylene isomers

• p –xylene can be separated from a mixture by cooling to -20 ºC to -75ºC.

Melting point

p-xylene +13.3

o-xylene -25.2

m-xylene -47.9

ethylbenzene -95.0

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Adsorption

• Depends upon selective adsorption on a column, followed by desorption

• Molecular sieves = zeolites = alumino-silicates having different pore size

• UOP process involves selective adsorption of p-xylene ( from a C8 stream) followed by desorption

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p-Xylene

• 7 billion pounds

• BP-Amoco the biggest with 4.6 billion pounds of U.S. capacity

• Virtually all goes to production of terephthalic acid and dimethyl terephthalate

CH3

CH3

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CH3

CH3

COOH

COOHp-xylene terephthalic acid

Air oxidation. Common catalysts are: CoBr2, MoBr2 or HBr

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COOH

COOH

terephthalic acid

OCH3O

OCH3Odimethylterephthalate

By esterification with methanol.

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TA & DMT

• Dupont Cape Fear plant makes terephthalic acid ( sold to Alpek, a Mexican petrochemicals group)

• Kosa ( Wilmington plant) makes terephthalic acid and dimethyl terephthalate

• Kosa makes about 1.5 billion pounds per year of dimethylterephthalate – largest in North America

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Cumene

+acid catalyst

cumene

8 billion pounds used in U.S.

Essentially all used for phenol production

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Cumene Capacity (million pounds) 8.7 Billion total

• Chevron Port Arthur, Tex. 1,000• Citgo Petroleum, Corpus Christi, Tex. 1,100• Coastal Eagle Point, Westville, N.J. 140• Georgia Gulf, Pasadena, Tex. 1,500• JLM Chemicals, Blue Island, Ill. 145• Koch Petroleum, Corpus Christi, Tex. 1,500• Marathon Ashland, Catlettsburg, Ky. 800 • Shell Chemical, Deer Park, Tex. 1,100 • Sun, Philadelphia, Pa. 1,200

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Phenol from Cumene

cumene

OH

phenol

???

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+ O2

OO

H

1. H+

2. - H2O

O+

O

+

H2O

O

OHOH

+

O

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Sunoco Phenol PlantHaverhill, Ohio

•

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Kellogg Phenol Plants

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Phenol Uses

• 41 %: Bisphenol-A

• 28 % phenolic resins

• 13 % caprolactam

NO

OHHO

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Major Phenol Producers

• Sun, Shell, Dow, GE, and Georgia Gulf are major producers

• GE plant at 700 million pounds• JLM has a 95 million pound plant in Illinois

(same JLM that operates shipping in Wilmington)

• Current demand about 5 billion pounds• 0.62 pounds acetone per pound phenol

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Bisphenol-A

HO

OH+

O

+

HO OH

BPA

Cumene gives 1 mole of phenol per mole of acetone

BPA uses 2 moles of phenol per mole of acetone

Typically, phenol is in demand and acetone is a glut on the market

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On to bigger things!