Samik1,
Ratna Ediati2, and Didik Prasetyoko3
Proceeding of International Conference On Research, Implementation And Education
Of Mathematics And Sciences 2014, Yogyakarta State University, 18-20 May 2014
Of Mathematics And Sciences 2014, Yogyakarta State University, 18-20 May 2014
1Chemistry
Department, Mathematical and Natural Sciences Faculty,
Surabaya State University (samikunesa@gmail.com, Tel.: +6285731160005), Indonesia
2,3Chemistry Department, Mathematical and Natural Sciences Faculty,
2,3Chemistry Department, Mathematical and Natural Sciences Faculty,
Institute of Technology Sepuluh Nopember, Indonesia
Abstract
Synthesis
of NaZSM-5 and impregnation of K3PO4 catalyst with concentration 5, 10, and 15 wt.% on the resulting NaZSM-5 as a
catalyst to produce biodiesel have been done in this study. This study
is an experimental study, the research stages include the synthesis and
characterization NaZSM-5 and K3PO4/NaZSM-5.
Characterization by X-Ray Diffraction (XRD) was conducted to determine the
X-ray diffraction patterns and the percentage crystallinity of the samples.
X-ray diffraction pattern of the resulting sample showed the emergence of
diffraction peaks with high intensity at 2θ = 7.8; 8.8; 23.0; 23.2, and 24.3°
are specifically indexed to the structure of the MFI topology. The percentage
crystallinity of the sample becomes smaller with increasing number of K3PO4
impregnated on NaZSM-5 synthesis. Characterization of the samples by Fourier
Transform Infra Red (FTIR) aims to determine the type of functional groups
present in a compound. FTIR spectra of samples NZ, NZK5, NZK10 and NZK15 have
absorption bands in the region 1220 and 547 cm-1 which shows the
absorption characteristics of vibration T - O - T on NaZSM-5 type zeolite which
distinguish the other and sensitive to changes in structure. The results of characterization using XRD and
FTIR showed that the structure of NaZSM-5 remained unchange after impregnated
with K3PO4.
Keyword: K3PO4/NaZSM-5,
the diffraction
pattern, the percentage crystallinity,
absorption characteristics
INTRODUCTION
Biodiesel, a mixture of fatty
acid alkyl esters, has been developed as one of the most promising alternative
fuel for fossil fuels regarding the limited resources of fossil fuels and the
environmental concerns [1]. Almost all commercial biodiesel is currently
produced by using homogeneous catalyst (i.e., KOH, NaOH and H2SO4).
Even though homogeneous catalyzed biodiesel production processes are relatively
fast and achieve high conversions, the removal of the homogeneous catalyst
after reaction may be a significant problem. This is a concern, since aqueous
quenching causes the formation of stable emulsions and saponification, making
separation of alkyl-esters difficult, resulting in the generation of large
amounts of waste water, and need a high
cost in operation especially for waste water treatment [1-3]. For this reason,
heterogeneous catalyst is likely to be used replacing homogeneous catalyst in
the near future.
Heterogeneous base catalysts are
more effective than acid catalysts and enzymes. From the economic standpoint,
it would be ideal if solid base catalysts could work efficiently at
temperatures below 150oC and low pressure. On the other hand, solid
acid catalysts, enzymes and non-catalytic supercritical transesterification
have been largely ignored in biodiesel research due to pessimistic expectations
in terms of reaction rates, undesirable side reactions and high costs [4].
Several heterogeneous base catalysts that
used for biodiesel production are ZnO-Al2O3/ZSM-5 yield
99,00% [2], K3PO4 yield 97,30% [5], KF/Ca-Al hidrotalcite
yield 97,14% [6], Mg/MCM-41 yield 85,00%
[7], KI/ mesoporous silica yield 90,09% [3]. In this experiment, K3PO4
is chosen as catalysts
because yield of biodiesel 97,30%, relatively insoluble in methanol and oil [5]. NaZSM-5 supported K3PO4 were prepared by
impregnation. Thus
the aim of this work is to evaluate character of NaZSM-5 and K3PO4/NaZSM-5
by XRD and FTIR.
RESEARCH METHOD
Synthesis
The
NaZSM-5 crystals were prepared by procedure similar to that described by Khalifah [8]. The seeding gels
were prepared by dissolving 1.28 gram sodium
aluminate in a solution (12.6 mL TPAOH and 62.5 mL water). After its complete dissolution, 28.2 ml TEOS was added in a
solution. This solution was stirred for
15 min and heated at 60 oC for 6 h. After gel formed, was added
11.952 gram CTABr little by little and was stirred until its complete
dissolution. Subsequently the crystallisation of the seeding gels was carried
out using autoclave for 24 h at 150 oC. Finally the solid was
separated by filtration, washed with distilled water until pH neutral and
dried, firstly for 24 h at 60 0C and subsequently for 24 h at 110 0C.
The occluded surfactant (CTA+) and the organic template (TPA+)
were removed by calcination in air at 550 oC for 10 h.
The K3PO4
solution was impregnated on NaZSM-5 by impregnation with concentration of K3PO4 at 5, 10, and 15 wt.%.
The catalyst was dried at 110 °C for 24 h followed by calcining at 550 °C for 10
h so that produce K3PO4/NaZSM-5
catalyst.
The
resulting NaZSM-5 and K3PO4/NaZSM-5 catalyst with concentration of K3PO4 at 5, 10, and 15 wt.%
are labeled NZ, NZK5, NZK10 and NZK15.
Characterisation
The
X-ray diffraction patterns and the percentage of crystallinity of NZ, NZK5, NZK10 and NZK15
were characterized by Phillips Expert X-Ray Diffraction (XRD) with Cu Ka radiation (40 kV, 30 mA) at scale 2θ = 5-40o and rate of scan 0,04
o/second. The infrared spectra were
recorded using the KBr pellets and Shimadzu Instrument Spectrum One 8400S Fourier Transform Infrared (FTIR)
Spectrometer in the range between 4000 and 400 cm-1.
RESULT AND DISCUSSION
X-ray
Diffraction
The X-ray diffraction pattern of K3PO4,
the resulting samples (NZ, NZK5, NZK10 and NZK15) and ZSM-5 was producted by Zhu et al. [9]
are shown in Fig. 1. The XRD pattern of the resulting
sample showed the emergence of diffraction peaks that similar with high intensity
at 2θ = 7.8; 8.8; 23.0; 23.2, and 24.3°.
This
XRD resulting is similar as the XRD patterns of ZSM-5 was reported by Zhu et al. [9] with high intensity at 2θ = 7.8;
8.8; 23.1; 23.4, and 24.4° are specifically indexed to the structure of the MFI
topology. On the basis of this characterization, NZ, NZK5, NZK10 and NZK15 included the
structure of the MFI topology and not be found the another ZSM-5 type.
Fig. 1 also show diffraction
pattern of the K3PO4 with high intensity at 2θ = 31.80.
The presence of K3PO4 impregnated on NaZSM-5
does not show new peak of K3PO4 at NZ, NZK5,
NZK10 and NZK15, suggesting that the structure of NaZSM-5 is not destroyed during the process of catalyst
preparation and K3PO4
has well dispersed on NaZSM-5. Zhang et al. [10] observe nothing diffraction peak of PtSnNa catalyst after impregnated on ZSM-5, suggesting that the structure of ZSM-5 is not destroyed during the process of catalyst
preparation. Some parts of Na+ and Sn4+ could enter the
zeolite main channels, while Pt particles were located mainly on the external
surface of the zeolite.
Fig. 1. The X-ray diffraction pattern of K3PO4, the resulting samples (NZ, NZK5, NZK10 and NZK15) and ZSM-5 was producted by Zhu et al. [9]
The intensities of NaZSM-5 characteristic peaks were decreasing caused by increasing of K3PO4 concentration. The phenomenon decreasing of the intensities of ZSM-5 characteristic peaks also reported by Kim et al. [2] after ZnO-Al2O3 and SnO-Al2O3 was impregnated on ZSM-5.
Table 1 show relationship
percentage crystallinity with percentage K3PO4
impregnated
on NaZSM-5, that calculated based on intensity main peak at 2θ = 23° using highest intensity sample (NaZSM-5) as comparator
standard that assumed has percentage crystallinity = 100. The percentage
crystallinity of the samples becomes smaller with increasing number of K3PO4
impregnated on NaZSM-5 synthesis.
Table 1. Relationship percentage
crystallinity with percentage K3PO4 impregnated on NaZSM-5
Sample
|
2θ
|
Intensity, I
|
I/Io
|
% Crystallinity
|
NZ
|
23.10
|
376.70*
|
1.00
|
100
|
NZK5
|
23.00
|
334.18
|
0.89
|
89
|
NZK10
|
23.01
|
314.18
|
0.83
|
83
|
NZK15
|
23.00
|
271.50
|
0.72
|
72
|
*
comparator standard (Io)
FTIR Spectra
FTIR spectra between
400–1300 cm-1 of K3PO4 and the resulting
samples (NZ,
NZK5, NZK10 and NZK15) are shown in Fig. 2. In this range all resulting samples possess
one broad band at 1000–1200 cm-1, and three bands around 795, 547,
and 455 cm-1. FTIR spectra of samples NZ, NZK5, NZK10 and NZK15 have
absorption bands in the region 1220 and 547 cm-1 which shows the
absorption characteristics of vibration T-O-T on NaZSM-5 type zeolite which
distinguish the other and sensitive to changes in structure.
Fig. 2. FTIR spectra of K3PO4 and the resulting samples (NZ, NZK5, NZK10 and NZK15)
Traditionally [8,11], the bands in the range at around 1000–1200 and 455 cm-1 are attributed to the structure insensitive internal tetrahedron asymmetric stretching vibrations T-O-T and bending vibrations Si-O-Si, respectively. The band at around 795 cm-1 can be attributed to both structure insensitive internal tetrahedron and structure sensitive external tetrahedron symmetric stretching vibrations Si-O-Si. The structure sensitive band, appearing in the presented spectra around 547 cm-1, is attributed to five-ring units in the structures of pentasil zeolites like ZSM-5 (Table 2).
FTIR
spectra of K3PO4 have absorption bands in the
region 1396, 1000 and 551 cm-1. The bands at 1396 and 879 cm-1 is attributed to vibrations of carbonate ion from CO2 gas adsorbed by K3PO4
[12-14]. The bands at
1000 and 551 cm-1 is attributed to stretching vibrations and bending
vibrations of phosphate ion on K3PO4
[12].
Building
on FTIR spectra, the presence of K3PO4 impregnated on NaZSM-5 does not show new bands of K3PO4 at NZ, NZK5, NZK10 and NZK15. So, the analysis resulting of characterization
using XRD and FTIR show that the structure of NaZSM-5 remained unchange after
impregnated with K3PO4.
Table
2. Wave number of of
K3PO4, ZSM-5 and the resulting samples
(NZ, NZK5, NZK10 and NZK15)
Bands
|
Wave number (cm-1)
|
Absorption
characteristics
|
|||||
K3PO4
|
ZSM-5
Gonçalves, et al [11]
|
NZ
|
NZK 5
|
NZK 10
|
NZK 15
|
||
V1
|
1396
|
-
|
-
|
-
|
-
|
-
|
Vibrations of carbonate ion
|
V2
|
1014
|
-
|
-
|
-
|
-
|
-
|
Stretching vibrations of
phosphate ion
|
V3
|
879
|
-
|
-
|
-
|
-
|
-
|
Vibrations of carbonate ion
|
V4
|
551
|
-
|
-
|
-
|
-
|
-
|
Bending vibrations of phosphate
ion
|
V5
|
-
|
1220
|
1222
|
1219
|
1215
|
1215
|
Structure insensitive internal
tetrahedron asymmetric stretching vibrations T-O-T
|
V6
|
-
|
1100
|
1103
|
1103
|
1099
|
1099
|
Structure insensitive internal
tetrahedron asymmetric stretching vibrations Si-O-T
|
V7
|
-
|
795
|
802
|
795
|
795
|
795
|
Structure insensitive internal
tetrahedron and structure sensitive external tetrahedron symmetric stretching
vibrations Si-O-Si
|
V8
|
-
|
546
|
547
|
547
|
548
|
548
|
Five-ring units in the
structures of pentasil
|
V9
|
-
|
450
|
455
|
455
|
459
|
459
|
Bending vibrations Si-O-Si
|
CONCLUSION AND SUGGESTION
Characterization by XRD and FTIR of the NaZSM-5 and K3PO4/NaZSM-5
catalyst
with
concentration of K3PO4 at 5, 10, and 15 wt.%
was investigated. The
XRD pattern of the resulting sample (NZ, NZK5, NZK10 and
NZK15) showed the emergence of diffraction peaks that
similar with high intensity at 2θ = 7.8; 8.8; 23.0; 23.2, and 24.3° that are
specifically indexed to the structure of the MFI topology and not be found the
another ZSM-5 type. The percentage crystallinity of the sample becomes smaller
with increasing number of K3PO4 impregnated on NaZSM-5
synthesis. FTIR spectra of resulting samples
have absorption bands in the region 1220 and 547 cm-1 which
shows the absorption characteristics of vibration T-O-T on NaZSM-5 type zeolite
which distinguish the other and sensitive to changes in structure. The analysis resulting of characterization
using XRD and FTIR show that the structure of NaZSM-5 remained unchange after
impregnated with K3PO4.
REFERENCES
[1] Zhang, L.,Sun, S., Xin, Z., Sheng, B. and
Liu, Q., (2010), “Synthesis and Component Confirmation of Biodiesel from Palm
Oil and Dimethyl Carbonate Catalyzed by Immobilized-Lipase in Solvent-Free
System”, Fuel, Vol. 89, 3960–3965.
[2] Kim, M., Yan, S., Salley, S.O. and Ng,
K.Y.S., (2009), “The Effect of Sodium on Catalytic activity of ZnO-Al2O3/ZSM-5
and SnO-Al2O3/ZSM-5 for tranesterification of vegetable
oil with methanol”, Catalysis Communication, Vol. 10, 1913-1919.
[3] Samart, C., Sreetongkittikul, P., and Sookman,
C., (2009), Heterogeneous Catalysis of Transesterification of Soybean Oil Using
KI/Mesoporous Silica, Fuel Processing Technology, Vol. 90, 922–925.
[4] Helwani, Z., Othman, M.R., Aziz, N., Kim, J.
and Fernando, W.J.N., (2009), “Solid heterogeneous catalysts for
transesterification of triglycerides with methanol: A review”, Applied
Catalysis A: General, Vol. 363, 1–10.
[5] Guan, Guoqing,
Kusakabe, Katsuki, and Yamasaki, Satoko, (2009), Tri-Potassium Phosphate
as A Solid Catalyst for Biodiesel Production from Waste Cooking Oil, Fuel
Processing Technology, Vol. 90, 520–524.
[6] Gao, Lijing, Teng, Guangyuan, and Wei,
Ruiping, (2010), Biodiesel from Palm Oil Via Loading KF/Ca – Al Hydrotalcite
Catalyst. Biomass and Bioenergy, Vol. 34, 1283 – 1288.
[7] Georgogianni, K.G., Katsoulidis, A.P.,
Pomonis, P.J., and Kontominas, M.G., (2009), Transesterification of Soybean
Frying Oil to Biodiesel Using Heterogeneous Catalysts, Fuel Processing
Technology, Vol. 90, 671–676.
[8] Khalifah,
S.N., (2010), Sintesis Katalis ZSM-5 Mesopori dan Aktivitasnya pada
Esterifikasi Minyak Jelantah untuk Produksi Biodiesel, Tesis, Institut
Teknologi Sepuluh November, Surabaya.
[9] Zhu,
H., Liu, Z., Kong, D., Wang, Y., Yuan, X. and Xie, Z., (2009), “Synthesis of
ZSM-5 with Intracrystal or Intercrystal Mesopores by Polyvinylbutyral
Templating Method”, Journal of Colloid
and Interface Science, Vol. 331, 432–438.
[10] Zhang, Y., Zhou, Y.,
Li, Y., Wang, Y., Xu, Y., and Wu, P., (2007), “Effect of Calcination
Temperature on Catalytic Properties of PtSnNa/ZSM-5 Catalyst for Propane
Dehydrogenation”, Catalysis
Communications, Vol. 8, 1009–1016.
[11] Gonçalves, M.L., Dimitrov, L.D., Jordao, M.H, Wallau, M
and Urquieta-Gonzalez, E.A., (2008),
“Synthesis of Mesoporous ZSM-5 by Crystallisation of Aged Gels in The Presence
of Cetyltrimethylammonium Cations”,
Catalysis Today, Vol. 133–135, 69–79.
[12] Pye, C.C. and
Rudolph, W.W., (2003), “An Ab Initio, Infrared, and Raman Investigation of
Phosphate Ion Hydration”, J. Phys. Chem.
A, Vol. 107, 8746-8755
[13] Nakamoto, K.,
(1978), Infrared and Raman Spectra of
Inorganic and Coordination Compounds,
Third Edition, John Wiley & Sons, Inc., New York.
[14] Silverstein,
Bassler, Morril, (1984), Penyidikan Spektrometrik Senyawa Organik, Erlangga,
Jakarta


Tidak ada komentar:
Posting Komentar