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Chemical and Process Engineering Research                                                                www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

                          Synthesis of Zeolite ZSM3 from Faujasite:
                Effects of Post-synthesis Ageing and Insitu seeding.

  Olusegun. A. Ajayi1* Abdulaziz Atta1 Benjamin.O. Aderemi1 Abdulkarrem. S. Ahmed1 Mku.T. Ityokumbul2 and
                                                    Sam.S.Adefila3


           1.   Department of Chemical Engineering, Ahmadu Bello University, Zaria. Kaduna State. Nigeria
                     2.   Department of Energy and Mineral Engineering, Penn State University, USA.
                3.   Department of Chemical Engineering, Covenant University, Ota. Ogun State. Nigeria
   *E-mail and telephone for corresponding author: segeaj@gmail.com +2348033175209 and +2348054288244


  This research work was sponsored by Petroleum Technology Developed Fund under the innovative domiciliation
                                                science program (2006)


ABSTRACT

The crystallization of ZSM3 via faujasite metamorphosis, synthesized from dealuminated metakaolin, was achieved
without the addition of any structure directing agent. The XRD, XRF, and SEM/EDXS analyses carried out on the
sample indicated successful synthesis of matrix, containing zeolites X, Y and sodium aluminosilicate, in various
proportions, which was later transformed completely into ZSM3. The XRD peaks and SEM morphologies attributed
to ZSM3 increased in intensity and crystallinity, as reaction and ageing time progressed. Post synthesis effects i.e.
exposure to dampness and longer contact time in the presence of residue/unwashed NaOH used for the synthesis
earlier, were totally responsible for the metamorphosis. Anatase and quartz were observed to persist in the raw,
intermediate and as-synthesized product, pointing to their high level of resistances to treatments. The formation of
competitive zeolite phases, was prevented by controlling factors responsible for its nucleation and formation.

Keywords: metamorphosis, insitu seeding, kaolin, ZSM3, faujasite, dealumination, aging

    1.   Introduction

Zeolites are advanced materials of crystalline silicates and aluminosilicates linked through oxygen atoms, producing
a three-dimensional network containing channels and cavities of molecular dimensions. Some recently known
materials which are structurally identical to the classical zeolite, but consisting of structural oxide other than silica
and alumina have extended this definition.

ZSM3, possessing 10 ring and 8 ring aluminosilicate framework with defined channel structures, has been widely
used in many catalytic reactions as catalysts owing to its excellent catalytic property and shape selectitvity (Perez-
Pariente et al,1988). ZSM3 was first synthesized by Plank et al (1977) in an aqueous system, using ethylenediamine

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Chemical and Process Engineering Research                                                              www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

or pyrrolindine as template. Wenyang et al (1982) studied the kinetics of ZSM3 crystallization and also reported on
the synthesis of zeolite ZSM3 in the system ethylenediamine-Na2O-Al2O3-SiO2-triethylamine (Wenyang et al, 1989),
with the possibility of recycling the organic compound to reduce cost and pollution. In 2004, Xuewu et al,
synthesized zeolite ZSM35 by vapor phase transport method in the system of NH4F -Al2O3-SiO2- ethylenediamine-
H2O, with good result and reduced consumption of organic materials. There exist various other reports in patents on
synthesis of ZSM3 (US Pat. 4107195 (Rollman, 1978), US Pat. 4,584,286 (Valyocsik, 1986), and PCT/US90/03827
(Rubin, 1989)), inter-alia.

The application of ZSM3 in variety of life makes its continuous synthesis imperative. Furthermore, recent
environmental protection concerns discourage the use of organic template; accordingly the need arise to opt for
alternative more economical and ecofriendly means of its synthesis.

Various researchers in this field reported formation of zeolite ZSM family series from prolonged aging method using
soluble salts as source of silica and alumina. Wulff-Dӧring and Lechert (1991) reported on co-crystallization of
zeolite Y and ZSM-3, while Rubin et al (1978) and Dwyer et al (1981) during the synthesis of ZSM34 and ZSM39,
showed that crystallization time of 98 and 90 days are required, respectively. They also claimed that the period for
crystallization reduces with increase in crystallization temperature. The work of Rosinski et al (1992), though on
synthesis of zeolite ZSM45, confirmed the aforementioned claim, and further shed more light on the metastability of
zeolite materials.

The rate at which the metastable faujasite zeolite changes to an equilibrium stable material is dependent upon
intrinsic properties of the zeolite, level of impurities in the gangue liquor and the chemical environment in which it
exists and aging period (Breck, 1974). For example, if zeolite A, after crystallization, is allowed to remain in its
mother liquor, it will recrystallize to zeolite P. Changes in the composition of amorphous reaction mixture, sources
of silica and alumina, inherent impurities, temperature and time of crystallization, have been identified as promoter
of recrystallization of zeolite X and Y to zeolite P and subsequently, analcime (Dwyer and Chu, 1979).

Dwyer and Chu (1979) were the first to report on metamorphosis of faujasite zeolite into ZSM4, using pure
analytical soluble salts as reagents. The work presented here treats transformation of impure kaolinite based faujasite
into zeolite ZSM3 promoted by only post-synthesis aging and insitu seeding.




    2.   Experimental
    2.1 Kaolin Pretreatment

The beneficiation of kaolin from Kankara (a village in Katsina State, Nigeria) was done as reported by Emofurieta et
al (1992). The beneficiated kaolin was calcined to metakaolin, for enhanced reactivity (Caballero et al,2007 and
Zheng et al,2005). The calcination was done at 9000C for 3hrs in a furnace. The silica-alumina (SiO2/Al2O3) molar


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Chemical and Process Engineering Research                                                             www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

ratio of 9 required for the desired zeolite was obtained by dealumination process. The dealumination was done using
98% H2SO4, for ten minutes, in a reflux condenser. The product obtained was washed with hot deionized water to
near neutrality, dried at 400C for 24hrs and later at 1250C in an electric oven, for another 24hrs. The compositional
analysis was carried out using EDXS and X-Ray fluorescence machine (model PW1660 X-ray analyzer), while the
structural pattern was observed on D500 X-ray diffractometry machine. The morphological analysis was done using
Jeol, JSM 5800.




    2.2 Gelation and Zeolite Formation

The dealuminated sample was mixed with calculated amount of NaOH to obtain a reaction mixture consisting of
SiO2/Al2O3=9, Na2O/ SiO2=0.6 and H2O/ Na2O=45. The resulting gel was left to age for 5 days at room temperature
in an airtight polypropylene bottle. At the end of the aging period, the gel was heated in an autoclave (WS2-84-64
model-7101) set at 1000C, for 24hrs. The resulting product was washed thoroughly with deionized water, to remove
excess sodium hydroxide and dried at 900C for 3hrs. Thereafter, the thus obtained product was divided into two
parts. A part was characterized immediately, while the other part was post-aged for 95 days under ambient
conditions, prior to analyses.

    3.   Results and Discussions


    3.1 Kaolin Beneficiation, Calcination and Dealumination

The compositional analysis indicated in Table 1 combined with the crystallographic analysis (Figure 1) revealed that
the raw kaolin contains associated impurities, i.e. muscovite, quartz, clinochlore and gmelinite, resulting in
SiO2/Al2O3 ratio of 2.55, as against SiO2/Al2O3 ratio of 2, for theoretical kaolin. The presence of fibrous layers in
between the silica-alumina plates as shown in Figure 2(a), further justifies this claim.

The effect of beneficiation (even though marginal with respect to bulk compositional changes, shown in Table 1),
was able to reduce muscovite, quartz, and gmelinite beyond the XRD detection limit, as depicted in Figure 3.

The phase transformation of kaolin into a more reactive one (i.e. semi-amorphous) was achieved via calcinations as
reflected in Figures 2(b) and Figure 4. It was observed that the kaolinite structure further decomposed into less
crystalline phases via dealumination and gellation (Figures 2c and d referred).

Oxides of potassium and iron were known to respectively, promote formation of zeolite P or D, in place of zeolite Y
and retard the growth and nucleation of zeolite Y (Murat et al,1992 ). Accordingly, particular attention was paid to
monitoring these oxides, as can be seen in Table 1. The two oxides were observed to reduce with increase in mode of
pretreatment, i.e. both physical and chemical method of beneficiations. Dealumination process targeted at improving
the SiO2/Al2O3 molar ratio also assisted in reducing the amounts of impurities in the sample as shown in Table 1 and

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Chemical and Process Engineering Research                                                                 www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

Figure 2(c). Figure 2 (c) further shows a breakdown of the metakaolinite structure, as result of acid attack. Evidently,
the silica-alumina plate-like-sheet observed earlier in the SEM picture apparently disappeared in Figure 2 (c).

The SiO2/Al2O3 ratio was deliberately kept relatively low, i.e. 9, in order to avoid co-crystallization of zeolite P – a
readily formed zeolite from high silica content than zeolite A or X (Breck, 1974). The Na2O/Na2O+K2O ratio was
determined from Table 1 and found to be very close to unity making the gel a potential ingredient for not only zeolite
X but also zeolite Y synthesis (Ruren et al, 2007).

    3.2 Faujasite Synthesis and Characterization

The XRD pattern for the fresh product analyzed (Figure 5) confirmed synthesis of mixed crystalline phases
quantitatively determined as: zeolite X (39.37%), zeolite Y (13.01%), quartz (13.13%), anatase (8.22%) and
unnamed zeolite (6.56%). This unnamed zeolite was confirmed through further analysis to be ZSM3. The SEM
pictures (Figure 2e) in agreement with the XRD analysis gave insight to the formation of the above named materials.
The tetragonal crystallite was attributed to presence of anatase, cubic to faujasite and the ZSM3 zeolite, while the
hexagonal, for quartz.

This observation is in agreement with the work reported by Chandrasekhar and Pramada (1999) and Erdem and Sand
(1979), on the formation of multiphase zeolite crystalline products from heterogeneous aluminosilicates as against
the use of soluble active silicates and aluminates that often result in formation of pure single phase zeolite.

    3.3 ZSM3 crystallization

Figure 6 shows the XRD patterns for the product obtained after 95 days of post synthesis aging of the second half
product. The pattern shows disappearance of peaks responsible for faujasite zeolite and increase in the intensity of
peaks attributed to ZSM3 zeolite. The anatase and quartz still persists and remained in the system, aside the
remaining unconverted sodium alumino-silicate that could serve as ingredient for further transistion. The results
obtained clearly substantiate the crystallization mechanism:       Amorphous → Faujasite → ZSM 3

The XRD analysis (Figure 5) shows the presence of unidentified zeolite in the matrix along with faujasite zeolites
which was later observed to transform almost completely into ZSM3 as ageing time progresses. The two main
mechanisms that have been proposed for zeolite crystallization have been from a “solid gel phase” or a “solution
phase”. In this case, it was suggested that the mechanism could have been a combination of both, with the solution
phase serving as the initiation stage leading to crystallization. The dried sample left to age for 95 days was not
calcined, enabling some intercalated water molecules present in the sample, which apparently were enough to further
the progress of the reaction. This observation is in agreement with reports of other researchers in this field who
claimed that zeolitic materials are metastable and continuously metamorphosis from one state to another, provided
there is a favourable condition and ingredient. For example Dwyen and Chu (1974) observed the transformation of
faujasite to ZSM4 although in the presence of templating agent. The transition noticed in the current report was


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Chemical and Process Engineering Research                                                              www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

achieved without the use of any templating agent but due to prolonged aging period. It was speculated that the
available un-depolymerized silica and unwashed/unconverted NaOH in the presence of dampness continue to react,
while the already formed faujasite in the system, serve as seeding agent for the autocatalytic reaction, as reported by
Hong-Jiang et al (2004). It should also be noted that ZSM3 zeolite is of the faujasite family (Breck, 1974) and a
relatively more stable phase of the family.

    4.   Conclusion

Kankara kaolinite clay provided the needed ingredients, i.e. silica and alumina for the successful synthesis of zeolite
X and Y matrix. The initially synthesized faujasite might have served as insitu seeding agent, catalyzing the
transformation process of faujasite to ZSM3 observed in this work. The XRD, SEM and XRD analyses depicted the
transformation of faujasite zeolite to ZSM3 (a relatively more stable state) without the need of organic template or
structure directing agent. This approach makes this route an economically and environmentally viable means of
ZSM3 synthesis.

    5.   References

Atta, A.Y. Ajayi, O. A. and Adefila, S.S. (2007). Synthesis of Faujasite Zeolites from Kankara Kaolin Clay. Journal
             of Applied Sciences Research, 3(10):1017-1021

Breck, D.W.( 1974). Zeolite Molecular Sieves, Structure, Chemistry and Use. John Wiley and Sons, New York.

Caballero, I. Colina, F. G. and Costa, J (2007). Synthesis of X-type zeolite from dealuminated kaolin by reaction
             with sulfuric acid at high temperature. Ind. Eng. Chem. Res. 46, 1029-1038

Chandrasekhar, S and Pramada, P. N. (1999). Investigation of the synthesis of zeolite NaX from Kerala kaolin.
             Journal of Porous Materials, 6(4), 283-297

Dwyer, F.G and Chu, P. (1979). ZSM4 crystallization via faujasite metamorphosis. Journal of Catalysis 59, 263-271

Dwyer, F.G. Chester, W. and Jenkins, E.E. (1981). Zeolite ZSM-39. US Pat. 4287166

Emofuriefa, W.O. Kayode, A.A. and Coker, S.A. (1992). Mineralogy, Geochemistry and Economic Evaluation of
             the kaolin deposits near Ubulu-Uku, Awo-Omana and Buan in Southern Nigeria. Journal of Mining and
             Geology, 28 (2), 211-220.

Erdem, A and Sand, L.B. (1979). Crystallization and metastable phase transformations of zeolite ZSM-5 in the
             (TPA)2O-Na2O-K2O-Al2O3-SiO2-H2O system. Journal of Catalysis. 60, 241-256.

Hong-Jiang, Yi., Wu. Tai-Liu, Wang, Li-Ping and Sun, Yao-Jun (2004). Synthesis of ZSM2 using NaX as seeds.
             Chinese Journal of Chemistry, 22, 126-130



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Chemical and Process Engineering Research                                                              www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

Murat, M. Amokrane, A. Bastide, J.P and Montanaro, L. (1992). Synthesis of zeolites from thermally activated
             Kaolinite, some observations on nucleation and growth. Clay Mineral, 27, 119-130

Perez-Pariente, J. Fornes, V. Martens, J.A. and Jacobs, P.A. (1988). Synthesis and Characterization of Zeolite ZSM3.
             Studies in Surface Science and Catalysis, vol. 37, 123-131

Plank, C.J. Rosinski, E.J. Rubin, M.K and Pa, B.C. (1977). Crystalline zeolite and method of preparing the same. US
             Pat.4,016,245 assigned to Mobil Oil Corporation

Rosinski, E.J and Rubin, M.K. (1992). Zeolite ZSM-45. US Pat. 5334367

Rubin, M.K. (1990). Synthesis of ZSM35. PCT/US90/03827 assigned to Mobil Oil Corporation.

Rubin, M.K. Cynwyd, B. Rosinski, E.J and Plank, C.J. (1978). Crystalline zeolite ZSM-34 and method of preparing
             the same. US Pat. 4086186

Valyocsik, E. W. (1986). Synthesis of Crystalline Silicate ZSM-35 assigned to Mobil Oil Corporation.

Wenyang, X. Jianquan, L. Wenyuan, L. Huiming, Z. and Bingchang, L (1989). “Non-aqueous synthesis of ZSM-35
             and ZSM-5. Zeolites, vol.9, 468-473

Wenyang, X. Jinxiang, D. and Jianquan, L (1990). Simultaneous crystallization of two dissimilar zeolites from the
       system ethylenediamine–Na2O–Al2O3–SiO2–H2O–triethylamine. J. Chem. Soc., Chem. Commun., 131-132.
       DOI: 10.1039/C39900000131

Wulff-Dӧring, J and Lechert, H. (1991). Investigation of the Crystallization of Y and ZSM-3 zeolites. Catalysis
             Today, vol.8. Issues 4, 395-404

Xu, R. Pang, W. Yu, J. Huo, Q and Chen, J (2007). Chemistry of Zeolites and related Porous Materials: Synthesis
             and Structure. John Wiley and Sons (Asia) Pte, Ltd.

Xuewu, L. Zhijuan, W. Hong, X and Jinxiang, D (2004). “The effects of F- on the synthesis of zeolite ZSM35 by a
             vapor phase transport method” accessed on www.chemistrymag.org/cji/2004/06a071pe.htm published
             on Oct. 1, vol.6. No 10, 71

Zheng, S. Shuhong, S. Zhang, Z. Gao, X. and Xu. X (2005). Effect of Properties of Calcined Microspheres of kaolin
             on the formation of NaY zeolite”. Bulletin of the Catalysis Society of India, 4, 12-17




                 Table 1: Compositional Analysis of the Samples

          Sample ID        RKK             BKK     MK 93        DMK            Gel    Zeo-Matrix        ZSM3



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Chemical and Process Engineering Research                                                      www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012

             Al2O3        32.2       35.2       36.2          14.8   15.5              20.3       24.4

              BaO         0.03       0.02       0.03          0.05   0.04              0.06       0.08
              CaO         0.15       0.14       0.15          0.11   0.10              0.16       0.16
             Fe2O3        3.16       2.28       2.28          1.69   0.64              0.89       0.74
              K 2O        1.26       0.68       1.31          0.32   0.20              0.28       2.15
             MgO          1.04       0.64       1.10          0.66   0.04              0.05       1.05
             MnO          0.09       0.04       0.06          0.01   -0.01             0.00       0.03
             Na2O         0.12       0.07       0.09          0.10   10.5              10.9       5.89
              SiO2        48.3       46.5       54.6          77.6   60.3              53.2       50.2
              TiO2        0.84       0.34       1.00          1.42   4.53              6.51       7.44
               SO3        0.09       0.09       0.06          0.16   3.50              0.24     0.010
              LOI        11.43      12.31       2.24          2.18   1.76               nd         nd
             Total        98.7       98.3       99.2          99.1   97.1              92.6       92.2
               Legend:

   RKK-Raw Kankara Kaolin               BKK-Beneficiated Kankara Kaolin      MK93-Metakaolin@9000C for 3hrs
   DMK-Dealuminated metakaolin          Gel-from metakaolin                  Matrix-zeolites X, Y and Unnamed




      Figure 1: XRD Pattern for Raw Kaolin


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Chemical and Process Engineering Research                                                     www.iiste.org
  ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
  Vol 3, 2012




   Figure 2: Scanning Electron Micrographs of (a) RKK, (b) MK93, (c) DMK93, (d) Gel, (e)Zeolite -Matrix and (f)
ZSM3




         Figure 3: XRD Pattern for Beneficiated Kaolin

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Chemical and Process Engineering Research                             www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012




       Figure 4: XRD Pattern for Kaolin calcined at 9000C for 3hrs.




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Chemical and Process Engineering Research                             www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012




       Figure 5: XRD Pattern for matrix/composite zeolitic material




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Chemical and Process Engineering Research               www.iiste.org
ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online)
Vol 3, 2012




               Figure 6: XRD Pattern for Zeolite ZSM3




                                                   39
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Synthesis of zeolite zsm3 from faujasite

  • 1. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Synthesis of Zeolite ZSM3 from Faujasite: Effects of Post-synthesis Ageing and Insitu seeding. Olusegun. A. Ajayi1* Abdulaziz Atta1 Benjamin.O. Aderemi1 Abdulkarrem. S. Ahmed1 Mku.T. Ityokumbul2 and Sam.S.Adefila3 1. Department of Chemical Engineering, Ahmadu Bello University, Zaria. Kaduna State. Nigeria 2. Department of Energy and Mineral Engineering, Penn State University, USA. 3. Department of Chemical Engineering, Covenant University, Ota. Ogun State. Nigeria *E-mail and telephone for corresponding author: segeaj@gmail.com +2348033175209 and +2348054288244 This research work was sponsored by Petroleum Technology Developed Fund under the innovative domiciliation science program (2006) ABSTRACT The crystallization of ZSM3 via faujasite metamorphosis, synthesized from dealuminated metakaolin, was achieved without the addition of any structure directing agent. The XRD, XRF, and SEM/EDXS analyses carried out on the sample indicated successful synthesis of matrix, containing zeolites X, Y and sodium aluminosilicate, in various proportions, which was later transformed completely into ZSM3. The XRD peaks and SEM morphologies attributed to ZSM3 increased in intensity and crystallinity, as reaction and ageing time progressed. Post synthesis effects i.e. exposure to dampness and longer contact time in the presence of residue/unwashed NaOH used for the synthesis earlier, were totally responsible for the metamorphosis. Anatase and quartz were observed to persist in the raw, intermediate and as-synthesized product, pointing to their high level of resistances to treatments. The formation of competitive zeolite phases, was prevented by controlling factors responsible for its nucleation and formation. Keywords: metamorphosis, insitu seeding, kaolin, ZSM3, faujasite, dealumination, aging 1. Introduction Zeolites are advanced materials of crystalline silicates and aluminosilicates linked through oxygen atoms, producing a three-dimensional network containing channels and cavities of molecular dimensions. Some recently known materials which are structurally identical to the classical zeolite, but consisting of structural oxide other than silica and alumina have extended this definition. ZSM3, possessing 10 ring and 8 ring aluminosilicate framework with defined channel structures, has been widely used in many catalytic reactions as catalysts owing to its excellent catalytic property and shape selectitvity (Perez- Pariente et al,1988). ZSM3 was first synthesized by Plank et al (1977) in an aqueous system, using ethylenediamine 29
  • 2. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 or pyrrolindine as template. Wenyang et al (1982) studied the kinetics of ZSM3 crystallization and also reported on the synthesis of zeolite ZSM3 in the system ethylenediamine-Na2O-Al2O3-SiO2-triethylamine (Wenyang et al, 1989), with the possibility of recycling the organic compound to reduce cost and pollution. In 2004, Xuewu et al, synthesized zeolite ZSM35 by vapor phase transport method in the system of NH4F -Al2O3-SiO2- ethylenediamine- H2O, with good result and reduced consumption of organic materials. There exist various other reports in patents on synthesis of ZSM3 (US Pat. 4107195 (Rollman, 1978), US Pat. 4,584,286 (Valyocsik, 1986), and PCT/US90/03827 (Rubin, 1989)), inter-alia. The application of ZSM3 in variety of life makes its continuous synthesis imperative. Furthermore, recent environmental protection concerns discourage the use of organic template; accordingly the need arise to opt for alternative more economical and ecofriendly means of its synthesis. Various researchers in this field reported formation of zeolite ZSM family series from prolonged aging method using soluble salts as source of silica and alumina. Wulff-Dӧring and Lechert (1991) reported on co-crystallization of zeolite Y and ZSM-3, while Rubin et al (1978) and Dwyer et al (1981) during the synthesis of ZSM34 and ZSM39, showed that crystallization time of 98 and 90 days are required, respectively. They also claimed that the period for crystallization reduces with increase in crystallization temperature. The work of Rosinski et al (1992), though on synthesis of zeolite ZSM45, confirmed the aforementioned claim, and further shed more light on the metastability of zeolite materials. The rate at which the metastable faujasite zeolite changes to an equilibrium stable material is dependent upon intrinsic properties of the zeolite, level of impurities in the gangue liquor and the chemical environment in which it exists and aging period (Breck, 1974). For example, if zeolite A, after crystallization, is allowed to remain in its mother liquor, it will recrystallize to zeolite P. Changes in the composition of amorphous reaction mixture, sources of silica and alumina, inherent impurities, temperature and time of crystallization, have been identified as promoter of recrystallization of zeolite X and Y to zeolite P and subsequently, analcime (Dwyer and Chu, 1979). Dwyer and Chu (1979) were the first to report on metamorphosis of faujasite zeolite into ZSM4, using pure analytical soluble salts as reagents. The work presented here treats transformation of impure kaolinite based faujasite into zeolite ZSM3 promoted by only post-synthesis aging and insitu seeding. 2. Experimental 2.1 Kaolin Pretreatment The beneficiation of kaolin from Kankara (a village in Katsina State, Nigeria) was done as reported by Emofurieta et al (1992). The beneficiated kaolin was calcined to metakaolin, for enhanced reactivity (Caballero et al,2007 and Zheng et al,2005). The calcination was done at 9000C for 3hrs in a furnace. The silica-alumina (SiO2/Al2O3) molar 30
  • 3. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 ratio of 9 required for the desired zeolite was obtained by dealumination process. The dealumination was done using 98% H2SO4, for ten minutes, in a reflux condenser. The product obtained was washed with hot deionized water to near neutrality, dried at 400C for 24hrs and later at 1250C in an electric oven, for another 24hrs. The compositional analysis was carried out using EDXS and X-Ray fluorescence machine (model PW1660 X-ray analyzer), while the structural pattern was observed on D500 X-ray diffractometry machine. The morphological analysis was done using Jeol, JSM 5800. 2.2 Gelation and Zeolite Formation The dealuminated sample was mixed with calculated amount of NaOH to obtain a reaction mixture consisting of SiO2/Al2O3=9, Na2O/ SiO2=0.6 and H2O/ Na2O=45. The resulting gel was left to age for 5 days at room temperature in an airtight polypropylene bottle. At the end of the aging period, the gel was heated in an autoclave (WS2-84-64 model-7101) set at 1000C, for 24hrs. The resulting product was washed thoroughly with deionized water, to remove excess sodium hydroxide and dried at 900C for 3hrs. Thereafter, the thus obtained product was divided into two parts. A part was characterized immediately, while the other part was post-aged for 95 days under ambient conditions, prior to analyses. 3. Results and Discussions 3.1 Kaolin Beneficiation, Calcination and Dealumination The compositional analysis indicated in Table 1 combined with the crystallographic analysis (Figure 1) revealed that the raw kaolin contains associated impurities, i.e. muscovite, quartz, clinochlore and gmelinite, resulting in SiO2/Al2O3 ratio of 2.55, as against SiO2/Al2O3 ratio of 2, for theoretical kaolin. The presence of fibrous layers in between the silica-alumina plates as shown in Figure 2(a), further justifies this claim. The effect of beneficiation (even though marginal with respect to bulk compositional changes, shown in Table 1), was able to reduce muscovite, quartz, and gmelinite beyond the XRD detection limit, as depicted in Figure 3. The phase transformation of kaolin into a more reactive one (i.e. semi-amorphous) was achieved via calcinations as reflected in Figures 2(b) and Figure 4. It was observed that the kaolinite structure further decomposed into less crystalline phases via dealumination and gellation (Figures 2c and d referred). Oxides of potassium and iron were known to respectively, promote formation of zeolite P or D, in place of zeolite Y and retard the growth and nucleation of zeolite Y (Murat et al,1992 ). Accordingly, particular attention was paid to monitoring these oxides, as can be seen in Table 1. The two oxides were observed to reduce with increase in mode of pretreatment, i.e. both physical and chemical method of beneficiations. Dealumination process targeted at improving the SiO2/Al2O3 molar ratio also assisted in reducing the amounts of impurities in the sample as shown in Table 1 and 31
  • 4. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Figure 2(c). Figure 2 (c) further shows a breakdown of the metakaolinite structure, as result of acid attack. Evidently, the silica-alumina plate-like-sheet observed earlier in the SEM picture apparently disappeared in Figure 2 (c). The SiO2/Al2O3 ratio was deliberately kept relatively low, i.e. 9, in order to avoid co-crystallization of zeolite P – a readily formed zeolite from high silica content than zeolite A or X (Breck, 1974). The Na2O/Na2O+K2O ratio was determined from Table 1 and found to be very close to unity making the gel a potential ingredient for not only zeolite X but also zeolite Y synthesis (Ruren et al, 2007). 3.2 Faujasite Synthesis and Characterization The XRD pattern for the fresh product analyzed (Figure 5) confirmed synthesis of mixed crystalline phases quantitatively determined as: zeolite X (39.37%), zeolite Y (13.01%), quartz (13.13%), anatase (8.22%) and unnamed zeolite (6.56%). This unnamed zeolite was confirmed through further analysis to be ZSM3. The SEM pictures (Figure 2e) in agreement with the XRD analysis gave insight to the formation of the above named materials. The tetragonal crystallite was attributed to presence of anatase, cubic to faujasite and the ZSM3 zeolite, while the hexagonal, for quartz. This observation is in agreement with the work reported by Chandrasekhar and Pramada (1999) and Erdem and Sand (1979), on the formation of multiphase zeolite crystalline products from heterogeneous aluminosilicates as against the use of soluble active silicates and aluminates that often result in formation of pure single phase zeolite. 3.3 ZSM3 crystallization Figure 6 shows the XRD patterns for the product obtained after 95 days of post synthesis aging of the second half product. The pattern shows disappearance of peaks responsible for faujasite zeolite and increase in the intensity of peaks attributed to ZSM3 zeolite. The anatase and quartz still persists and remained in the system, aside the remaining unconverted sodium alumino-silicate that could serve as ingredient for further transistion. The results obtained clearly substantiate the crystallization mechanism: Amorphous → Faujasite → ZSM 3 The XRD analysis (Figure 5) shows the presence of unidentified zeolite in the matrix along with faujasite zeolites which was later observed to transform almost completely into ZSM3 as ageing time progresses. The two main mechanisms that have been proposed for zeolite crystallization have been from a “solid gel phase” or a “solution phase”. In this case, it was suggested that the mechanism could have been a combination of both, with the solution phase serving as the initiation stage leading to crystallization. The dried sample left to age for 95 days was not calcined, enabling some intercalated water molecules present in the sample, which apparently were enough to further the progress of the reaction. This observation is in agreement with reports of other researchers in this field who claimed that zeolitic materials are metastable and continuously metamorphosis from one state to another, provided there is a favourable condition and ingredient. For example Dwyen and Chu (1974) observed the transformation of faujasite to ZSM4 although in the presence of templating agent. The transition noticed in the current report was 32
  • 5. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 achieved without the use of any templating agent but due to prolonged aging period. It was speculated that the available un-depolymerized silica and unwashed/unconverted NaOH in the presence of dampness continue to react, while the already formed faujasite in the system, serve as seeding agent for the autocatalytic reaction, as reported by Hong-Jiang et al (2004). It should also be noted that ZSM3 zeolite is of the faujasite family (Breck, 1974) and a relatively more stable phase of the family. 4. Conclusion Kankara kaolinite clay provided the needed ingredients, i.e. silica and alumina for the successful synthesis of zeolite X and Y matrix. The initially synthesized faujasite might have served as insitu seeding agent, catalyzing the transformation process of faujasite to ZSM3 observed in this work. The XRD, SEM and XRD analyses depicted the transformation of faujasite zeolite to ZSM3 (a relatively more stable state) without the need of organic template or structure directing agent. This approach makes this route an economically and environmentally viable means of ZSM3 synthesis. 5. References Atta, A.Y. Ajayi, O. A. and Adefila, S.S. (2007). Synthesis of Faujasite Zeolites from Kankara Kaolin Clay. Journal of Applied Sciences Research, 3(10):1017-1021 Breck, D.W.( 1974). Zeolite Molecular Sieves, Structure, Chemistry and Use. John Wiley and Sons, New York. Caballero, I. Colina, F. G. and Costa, J (2007). Synthesis of X-type zeolite from dealuminated kaolin by reaction with sulfuric acid at high temperature. Ind. Eng. Chem. Res. 46, 1029-1038 Chandrasekhar, S and Pramada, P. N. (1999). Investigation of the synthesis of zeolite NaX from Kerala kaolin. Journal of Porous Materials, 6(4), 283-297 Dwyer, F.G and Chu, P. (1979). ZSM4 crystallization via faujasite metamorphosis. Journal of Catalysis 59, 263-271 Dwyer, F.G. Chester, W. and Jenkins, E.E. (1981). Zeolite ZSM-39. US Pat. 4287166 Emofuriefa, W.O. Kayode, A.A. and Coker, S.A. (1992). Mineralogy, Geochemistry and Economic Evaluation of the kaolin deposits near Ubulu-Uku, Awo-Omana and Buan in Southern Nigeria. Journal of Mining and Geology, 28 (2), 211-220. Erdem, A and Sand, L.B. (1979). Crystallization and metastable phase transformations of zeolite ZSM-5 in the (TPA)2O-Na2O-K2O-Al2O3-SiO2-H2O system. Journal of Catalysis. 60, 241-256. Hong-Jiang, Yi., Wu. Tai-Liu, Wang, Li-Ping and Sun, Yao-Jun (2004). Synthesis of ZSM2 using NaX as seeds. Chinese Journal of Chemistry, 22, 126-130 33
  • 6. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Murat, M. Amokrane, A. Bastide, J.P and Montanaro, L. (1992). Synthesis of zeolites from thermally activated Kaolinite, some observations on nucleation and growth. Clay Mineral, 27, 119-130 Perez-Pariente, J. Fornes, V. Martens, J.A. and Jacobs, P.A. (1988). Synthesis and Characterization of Zeolite ZSM3. Studies in Surface Science and Catalysis, vol. 37, 123-131 Plank, C.J. Rosinski, E.J. Rubin, M.K and Pa, B.C. (1977). Crystalline zeolite and method of preparing the same. US Pat.4,016,245 assigned to Mobil Oil Corporation Rosinski, E.J and Rubin, M.K. (1992). Zeolite ZSM-45. US Pat. 5334367 Rubin, M.K. (1990). Synthesis of ZSM35. PCT/US90/03827 assigned to Mobil Oil Corporation. Rubin, M.K. Cynwyd, B. Rosinski, E.J and Plank, C.J. (1978). Crystalline zeolite ZSM-34 and method of preparing the same. US Pat. 4086186 Valyocsik, E. W. (1986). Synthesis of Crystalline Silicate ZSM-35 assigned to Mobil Oil Corporation. Wenyang, X. Jianquan, L. Wenyuan, L. Huiming, Z. and Bingchang, L (1989). “Non-aqueous synthesis of ZSM-35 and ZSM-5. Zeolites, vol.9, 468-473 Wenyang, X. Jinxiang, D. and Jianquan, L (1990). Simultaneous crystallization of two dissimilar zeolites from the system ethylenediamine–Na2O–Al2O3–SiO2–H2O–triethylamine. J. Chem. Soc., Chem. Commun., 131-132. DOI: 10.1039/C39900000131 Wulff-Dӧring, J and Lechert, H. (1991). Investigation of the Crystallization of Y and ZSM-3 zeolites. Catalysis Today, vol.8. Issues 4, 395-404 Xu, R. Pang, W. Yu, J. Huo, Q and Chen, J (2007). Chemistry of Zeolites and related Porous Materials: Synthesis and Structure. John Wiley and Sons (Asia) Pte, Ltd. Xuewu, L. Zhijuan, W. Hong, X and Jinxiang, D (2004). “The effects of F- on the synthesis of zeolite ZSM35 by a vapor phase transport method” accessed on www.chemistrymag.org/cji/2004/06a071pe.htm published on Oct. 1, vol.6. No 10, 71 Zheng, S. Shuhong, S. Zhang, Z. Gao, X. and Xu. X (2005). Effect of Properties of Calcined Microspheres of kaolin on the formation of NaY zeolite”. Bulletin of the Catalysis Society of India, 4, 12-17 Table 1: Compositional Analysis of the Samples Sample ID RKK BKK MK 93 DMK Gel Zeo-Matrix ZSM3 34
  • 7. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Al2O3 32.2 35.2 36.2 14.8 15.5 20.3 24.4 BaO 0.03 0.02 0.03 0.05 0.04 0.06 0.08 CaO 0.15 0.14 0.15 0.11 0.10 0.16 0.16 Fe2O3 3.16 2.28 2.28 1.69 0.64 0.89 0.74 K 2O 1.26 0.68 1.31 0.32 0.20 0.28 2.15 MgO 1.04 0.64 1.10 0.66 0.04 0.05 1.05 MnO 0.09 0.04 0.06 0.01 -0.01 0.00 0.03 Na2O 0.12 0.07 0.09 0.10 10.5 10.9 5.89 SiO2 48.3 46.5 54.6 77.6 60.3 53.2 50.2 TiO2 0.84 0.34 1.00 1.42 4.53 6.51 7.44 SO3 0.09 0.09 0.06 0.16 3.50 0.24 0.010 LOI 11.43 12.31 2.24 2.18 1.76 nd nd Total 98.7 98.3 99.2 99.1 97.1 92.6 92.2 Legend: RKK-Raw Kankara Kaolin BKK-Beneficiated Kankara Kaolin MK93-Metakaolin@9000C for 3hrs DMK-Dealuminated metakaolin Gel-from metakaolin Matrix-zeolites X, Y and Unnamed Figure 1: XRD Pattern for Raw Kaolin 35
  • 8. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Figure 2: Scanning Electron Micrographs of (a) RKK, (b) MK93, (c) DMK93, (d) Gel, (e)Zeolite -Matrix and (f) ZSM3 Figure 3: XRD Pattern for Beneficiated Kaolin 36
  • 9. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Figure 4: XRD Pattern for Kaolin calcined at 9000C for 3hrs. 37
  • 10. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Figure 5: XRD Pattern for matrix/composite zeolitic material 38
  • 11. Chemical and Process Engineering Research www.iiste.org ISSN 2224-7467 (Paper) ISSN 2225-0913 (Online) Vol 3, 2012 Figure 6: XRD Pattern for Zeolite ZSM3 39
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