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Light Alkanes to Aromatics: Bruce Gates, University of California, Davis

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(1)

Conversion of

C

2

& C

3

alkanes to aromatics

Starting points for discussion

existing technology (UOP Cyclar

TM

process)

catalysts

reported to be

metal-containing zeolites

•substantial

research reported

for such conversions

related

issue topic covered yesterday:

(2)

Thermodynamically, conversion of

propane to aromatics

less uphill than

methane to aromatics

reaction

Δ

G

400

(kJ/mol)

6 CH

4

C

6

H

6

+

9 H

2

399

(3)

REPORTED CATALYSTS

acidic zeolite (e.g., HZSM-5) or, better,

zeolite-supported metals such as

Zn, Ga,

Mo

(also used for methane conversion)

less than fully characterized

metals possibly present as carbides (or oxycarbides);

not in metallic state

(4)

catalysts rapidly coked

require frequent regeneration

regeneration might contribute to

catalyst deactivation

(5)

Source: www.uop.com/ cyclar- process- produces- high- quality - aromatic- products

UOP CyclarTM Process, developed by BP & UOP endot hermic

Sabic process operat ing in Saudi Arabia Light gas product s Feed propane

(6)

Source of figure: www.uop.com/cyclar-process-produces-high-quality -aromatic-products

SUGGESTED REACTION NETWORK

Numerous authors suggest dehydrogenation catalyzed by

metal-containing function (e.g., molybdenum carbide)—slow reaction—

(7)

Feed: propane and/or butane

Aromatic

(benzene, toluene, xylenes)

yields said to be

58-60%

H

2

product (may be ~5% yield)

Rapid

catalyst

deactivation

requires

“continuous” regeneration,

moving bed reactors

(catalyst residence time presumably of days)

Catalyst lifetime

said to be

not short

Source: www.uop.com/ cyclar- process- produces- high- quality - aromatic- products

(8)

Possible opportunities for discovery of improved catalysts

Metal-containing molecular sieves

Active for reactions including (de)hydrogenation

large & growing class of catalytic materials

many structurally nonuniform & less than well characterized

Catalytic performance depends strongly on structure of

metal-containing species

Synthetic routes allow some tuning of structure & catalytic properties

less common routes include

(9)

Example: Catalysts made by ALD with

dimethyl zinc

(among others)

Characterized by IR, NMR, XAS, TPR, …..

Reaction at atmospheric pressure, 823 K

Zinc species not simple (not molecular)

Are there good opportunities to make well-defined

species containing metals such as Zn, Ga, &/or Mo in

zeolites?

Single-site catalysts?

(10)

Candidate research directions

Vary

metal or combination of metals in molecular sieve

molecular sieve (& pore structure)

Attempt to tailor metal-containing catalytic sites

single sites on/in molecular sieve framework

multi-atom sites (clusters)

Understand chemistry of synthesis & catalysis

Relate catalytic activity, selectivity, stability to structure

(use theory, spectroscopy of functioning catalysts)

Deeper characterization of catalysts

(11)

Comparison process: Chevron Aromax

TM

Feed: alkanes such as n-hexane, n-heptane

Products: aromatics such as benzene & toluene

Catalyst: Pt clusters in LTL zeolite with exchange ions such as Ba2+ & promoters such as halides

This is naphtha reforming without the acidic function in the catalyst.

(12)
(13)

Referensi

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