characterization of clay based k catalysts

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  • 7/23/2019 Characterization of Clay Based K Catalysts

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    LS VT R

    Applied Catalysis A: General 132

    (

    1995) 141-155

    Characterization of clay-based K catalysts and their

    application in Friedel-Crafts alkylation of arom atics

    Tivadar Cseri a,b, Sfmdor B6kAssy a, Fraqois Figueras b,*,

    Eleonbra Cseke , Louis-Charles de Menorval

    ,

    Roger Dutartre

    echnical U niversi& of Budapest, Department ojOrganic Chem ica/ Technology, 1521 Budapest, Hungu)

    Institut de Recherche s SW la Catalyze du CNR S, 2 Avenue Albert Eimtein 69626, Villeurhanne Cedeu. France

    L&oratoire de Matdriaux Catalytiques et Catalyse erl C/like Organique, URA 4/K du CNR S, ENSC M, 8 rue

    de 1 Ecole Norm als, 340.53 Montpellier Cedex, France

    Received 20 April 1995: revised 27

    June

    1995; accepted 27

    July

    1995

    Abstract

    Toluene was alkylated with benzyl chloride and benzyl alcohol using a series of clays KSF, KSF/

    0, KO, KPI 0, KlO, KS from Siid Chemie) obtained by treating a bavarian bentonite by different acids

    and a Hungarian bentonite Mid) as catalysts in a batch reactor. The catalysts w ere characterized by

    chemical analysis, thermal analysis, nitrogen adsorption, solid state nuclear magnetic resonance, X-

    ray diffraction. The acidity of these solids was determined by infrared spectroscopy using pyridine as

    molecular probe. The structure. specific surface area, and distribution of Lewis/Br@nsted acidity of

    these clays can be changed to a great extent by acidic or thermal treatment. The rate of alkylation is

    related to BrGnsted acidity when the substrate is benzyl alcohol. When benzyl chloride is used as

    alkylating agent, the Fe+ content of the clay controls the activity, and iron containing clays show

    high activities in spite of their low Lewis acidities.

    Keywords: Aromatics; Alkylation: K catalysts; Acidic clays; Brensted acidity; Fe

    1 Introduction

    Solid acids offer many advantages by their nature, over soluble counterparts such

    as aluminium chloride and hydrogen fluoride. The substitution of liquid acids by

    solids as catalysts for organic synthesis offers a potential for superior effectiveness

    and environmental integrity. However the origin of their activity is generally poorly

    understood. Although they differ in structure from liquid acids, solid acid catalysts

    * Corresponding author. Tel. ( + 33) 72445300, fax. ( + 33) 72445300.

    0926-860X/95/ 09.50 0 1995 Elsevier

    Science

    B.V. All rights reserved

    SSDIO926-860X 95)00158-1

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    42 T. Cseri et al. /Applied Cutnl~sis A: Gmeral 132 1995) 141-155

    work by the same principle. Clays have been proposed as suitable c atalysts for this

    purpose [ l-31. Friedel-Crafts alkylation is one of the most important reactions in

    synthetic and industrial organic chem istry, thus an interesting model. The alkylation

    of toluene by benzyl chloride or benzyl alcohol is interesting for the preparation of

    substitutes of polychlorobenzenes used as dielectrics. These reactions are usually

    catalysed by Lewis acids in liquid phase [ 41 in homogeneous phase and an indus-

    trial process is based on FeCl,

    [ 51.

    In heterogeneous catalysis, zeolites [6]

    ,

    sulfated zirconia [7] and clays

    exchanged by metallic cations [8-l 1 ] have been described. Particulary good results

    have been obtained using as catalyst a zinc chloride impregnated on KlO mont-

    morillonite, called clayzic [ 12-161. Clark et al. [ 171 recently reviewed the work

    published on clays impregnated by zinc chloride, and activated at low temperature

    T KSF > KPlO > KS > KlO > KO > Bavarian bentonite,

    Hungarian bentonite.

    Indeed it is doubful that this scale of acidity in water is valid in organic solvents

    due to a different solvation of the acid sites. The adsorption of pyridine in the gas

    phase, followed by infrared spectrometry is probably more representative in that

    case. It also permits to establish the nature of the acid sites. The relative intensities

    of the bands of pyridine adsorbed on Bronsted and Lewis sites are reported in

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    148

    T. Cseri et al. /Applied

    Catdyh

    A: Grnerul 132 199.5) 141-155

    I

    ,

    ollm

    150

    I

    100

    I

    54

    I

    I

    0

    I

    -50

    1

    -100

    I

    -150

    1

    -200

    -250 -300

    Fig.

    3. Al MA 9 NMR

    spectrum of KPlO

    Table 6, assum ing that the vibrations at 1448-14 55 cm-

    are associated to pyridine

    coordinated to Lewis sites, and the vibration at 1545 cm- to pyridinium ions.

    Small shifts are observed in the bands of pyridine adsorbed on Lewis sites, but the

    magn itude of these shifts is not large enough to establish clear changes of the acid

    strength between the different solids.

    The intensities are normalized to the vibrations of the lattice in the spectral range

    1920 cm- and 1800 cm- . The patterns of acidity obtained by this method are:

    KS < KlO < KPlO < KSF < KSF/O, for Bronsted acidity and KPlO < KSF

    < K SF/O < KS < KIO for Lewis acidity. C ompared to the pattern obtained in

    Table 3

    Chemical shifts (ppm) of the different Si species observed on the K clays

    Catalyst

    Hungarian bentonite

    - 90.6

    Bavarian bentonite

    -90.9

    K10

    -90.7

    - 101.3

    - 110.5

    KO

    - 90.5

    - 101.1

    - 109.3

    KPIO

    -91.5

    - 102.0

    - 109.8

    KS

    - 90.6

    - 99.9

    - 109.8

    KSF

    -90.2

    KSFIO

    -91.0

    - 103.3

    - 108.6

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    T. Cseri et al. Appl ied Catal ysis A: General 132 1995) 141-155

    149

    Table 4

    Chemical shifts (ppm) of the different Al species observed on the K clays

    Catalyst a, tetrahedral

    a, tetrahedral

    i17 etrahedral

    ?I, octahedral

    Hungarian bentonite 61.3

    61.2 53.0

    2.5

    Bavarian bentonite 70.0

    55.5

    2.9

    KlO

    70.7

    3.6

    KO 72.7

    4.1

    KPlO 73.8

    3.9

    KS 71.7

    3.8

    KSF

    71.8

    56.8 3.7

    KSF/O 75.0

    Table 5

    pH of the suspension of the K catalysts (10% in

    w ater)

    Catalyst pH of 10% suspension

    Hungarian bentonite

    7

    Bavarian bentonite

    7

    K 10

    4.5

    KO

    5.5

    KPlO

    1.8

    KS

    3

    KSF

    1.5

    KSF/O

    1.3

    Table 6

    Relative intensities of the infrared bands of adsorbed pyridine on the clays dried at 393 K

    Catalyst Lewis acidity

    Br nsted acidity

    KlO

    1.91

    2.23

    KPlO

    0.42

    2.32

    KS

    1.02

    1.76

    KSF

    0.59

    2.35

    KSF/O

    0.61

    3.09

    water Bavarian bentonite, H ungarian bentonite < KO < KlO < KS < KPlO