1403846

advertisement
1
EFFECT OF GEL VOLUME IN AUTOCLAVE ON
2
HYDROTHERMAL SYNTHESIS OF MORDENITE
3
FROM RICE HUSK SILICA
4
5
Running head: Effect of gel volume on mordenite synthesis
6
7
Suriyan Rakmae and Jatuporn Wittayakun*
8
School of Chemistry, Institute of Science, Suranaree University of Technology, Nakhon
9
Ratchasima 30000, Thailand. Tel.: +66 44 224 256; Fax: +66 44 224 185.
10
Email: jatuporn@sut.ac.th
11
*Corresponding author
12
13
Abstract:
14
Silica prepared by refluxing rice husk with HCl acid followed by calcination
15
(refluxed RHS) and dissolution of rice husk ash followed by precipitation
16
(precipitated RHS) was used as a silica source for a synthesis of mordenite in
17
sodium form (NaMOR) by hydrothermal method. The gel volume in an
18
autoclave was 30, 50 and 70%. The NaMOR products from both silica
19
sources were analyzed by X-ray diffraction (XRD), X-ray fluorescence
20
(XRF), N2 adsorption-desorption, ammonia temperature programmed
21
desorption (NH3-TPD) and scanning electron microscopy (SEM). All samples
22
showed characteristic XRD peaks of NaMOR. The properties of the products
23
including Si/Al ratio, surface area, acidity and morphology were influenced
24
by gel volume in the autoclave and the silica source.
25
26
Keywords: Mordenite, hydrothermal synthesis, rice husk silica, reflux,
27
precipitation
28
29
Introduction
30
In several countries including Thailand, rice husk (RH) is produced in a large
31
quantity as a byproduct from rice milling. RH composes of about 20 wt% of
32
inorganic compound in which silica is a main component (about 85-98% wt%)
33
(Juliano et al., 1985). Several methods to obtain the silica from rice husk with
34
high purity are acid treatment of RH before cacination (Liou, 2004, Panpa and
35
Jinawath, 2009, Krishnarao et al., 2001) and dissolution RHA with alkali solution
36
before precipitation with acidic solution (Kalapathy et al., 2000). Silica from RH
37
is amorphous with a uniform dispersion by molecular unit, fine particle size, high
38
purity and surface area (Liou et al., 2011). Moreover, when RH is burned, rice
39
husk ash (RHA) with silica purity of 76-95 wt% was obtained depending on
40
conditions (Kordatos et al., 2008, Naskar et al., 2012, Tepamat et al., 2013). Silica
41
from leaching of RH and RHA can be used as a silica source for the synthesis of
42
silicon-based materials.
43
With high purity, RHS can be used as a silica source for the production of
44
porous inorganic materials such as zeolites LSX (Khemthong et al., 2007), NaY
45
(Wittayakun et al., 2008; Khabuanchalad et al., 2008) NaBEA (Loiha et al.,
46
2009), NaZSM-5 (Pimsuta et al., 2013) and MCM-41 mesoporous silica (Artkla et
47
al., 2008). Moreover, rice husk charcoal was used as a silica source for the
48
synthesis of zeolite NaA (Tepamat et al., 2013) and silicon carbide (SiC)
49
(Makornpan et al., 2013). The interest of this work was to use silica from rice
50
husk for the synthesis of zeolite mordenite (MOR).
51
MOR is a zeolite with interconnected pore channels between 12-
52
membered ring and 8-membered ring (Baerlocher and McCusker, www). The unit
53
cell dimensions of NaMOR were first reported by Meier (1961). It has a pore
54
channel between 12-membered ring in the c-axis and 8-membered ring in the b-
55
axis. Si/Al ratio of MOR can be varied depending on composition of the synthetic
56
batch (Roland and Kleinschmit, 2003). MOR has been used as a solid catalyst for
57
various industrial chemical reactions (Pantu et al., 2007).
58
Kulawong et al. (2011) reported a synthesis of NaMOR in sodium form
59
(NaMOR) using rice husk silica (RHS). They crystallized the NaMOR in a
60
Teflon-lined autoclave with 150 mL capacity at various time and used the optimal
61
condition for a synthesis with another autoclave with 250 mL capacity. However,
62
the void volume was not reported for both vessels. Thus, it is an aim of this work
63
to understand the influence of gel volume in an autoclave on physicochemical
64
properties of MOR. Moreover, an effect of the silica source from acid leaching
65
and from precipitation was studied.
66
67
68
Materials and Methods
69
Preparation of rice husk silica by reflux and calcination (RRHS)
70
RH was obtained from a local mill near Suranaree University of
71
Technology, Thailand. It was washed several times with tap water, soaked in DI
72
water for 10 min and dried at 70 ºC overnight. Twenty five grams of the dried rice
73
husk was filled in a 250-mL round bottom flask, added with 180 mL of 3 M HCl
74
solution (prepared from 37% HCl, Merck) and refluxed at 100 ºC for 6 h. The
75
refluxed rice husk was washed several times with tap water until pH of the wash
76
solution equaled to that of the tap water, soaked in DI water for 10 min, dried at
77
70 ºC overnight and calcined at 600 ºC for 6 h in a muffle furnace (CABOLITE)
78
with a heating rate of 2 ºC/min.
79
80
Preparation of rice husk silica by dissolution-precipitation (PRHS)
81
First, rice husk ash (RHA) was prepared by calcination of the dried RH at
82
600ºC in a muffle furnace with heating rate of 2 ºC/min and cooled to room
83
temperature. Four grams of RHA was dissolved in 100 mL NaOH solution
84
(Prepared from NaOH pellet (Merck) with RHA: NaOH weight ratio of 1:1.9) in
85
polyethylene bottle under magnetic stirring with a speed of 300 rpm for 36 h at
86
room temperature. Then, the solution was filtered through a filter paper (Whatman
87
No.1) by an aspirator to a polyethylene beaker, added with a 6 N H2SO4 solution
88
(Sigma Aldrich) dropwise from a burette until the pH was about 11. Then, the
89
solution was heated to 90-95 ºC with continuous addition of sulfuric acid.
90
Precipitation of silica began when the pH was about 10.5-10.6. Then, DI water
91
(50 mL) was added and the gel was broken by magnetic stirring. The H2SO4
92
solution was further added until the pH was 7 and the mixture was kept under
93
stirring at this condition for 3 h. The precipitated silica was separated by
94
centrifugation and washed repeatedly with warm DI water until the pH of washed
95
water equal to that of DI water. Then, the precipitated silica powder was dried at
96
120 ºC for 24 h in a hot air oven.
97
98
Synthesis of mordenite (MOR)
99
The NaMOR was synthesized with a procedure adapted from Kim and
100
Ahn (1991). Silica (either RRHS or PRHS) was suspended in DI water to form
101
slurry in a polypropylene bottle. Then, sodium aluminate (Riedel-de Haën®,
102
41.383% Na2O, 58.604% Al2O3) in NaOH solution was added under a magnetic
103
stirring (250 rpm) at room temperature to produce a gel with the following molar
104
ratio: 6Na2O:Al2O3:29.2SiO2:780H2O. The mixture was transferred to a Teflon-
105
lined stainless steel autoclave and crystallized at 170 ºC (with heating rate 2.5
106
ºC/min) without agitation for 120 h. The autoclave volume was 245 cm3 and the
107
percent of gel/autoclave volume was 30, 50 and 70%. The sample was named
108
according to the silica type and gel volume. For example, R-MOR-30 was the
109
product from refluxed RHS with volume 30% of the autoclave volume; P-MOR-
110
70 was the product from precipitated RHS with volume 70% of the autoclave
111
volume.
112
washed thoroughly with DI water and dried at 100 ºC overnight.
113
After crystallization, the product was separated by centrifugation,
114
Characterization
115
Phase of NaMOR was studied by an X-ray diffraction (XRD, Bruker AXS
116
D5005) with nickel-filtered Cu Kα radiation (wavelength = 1.54 Å) scanning in
117
the 2θ range of 5–50º, at an increment of 0.02º and scan speed of 1 s/step).
118
Elemental analysis was determined by X-ray fluorescence (XRF, Horiba
119
Scientific XGT-5200). Morphologies of the silica were studied by scanning
120
electron microscopy (SEM, JOEL/JSM-6010LV). All samples were coated with
121
gold by sputtering (Neocoater/mp-19020NCTR).
122
The surface area of obtained NaMOR was determined by N2 adsorption-
123
desorption analysis (Micromeritics ASAP 2010) from the Brunauer-Emmet-Teller
124
(BET) method in a relative pressure range of 0.01–0.2. Each sample was first
125
degassed at 300 ºC and the analysis was carried out at liquid nitrogen temperature.
126
The acidity of obtained NaMOR was determined by temperature-
127
programmed desorption of ammonia (NH3-TPD) in a Belcat-B equipped with a
128
thermal conductivity detector. A sample amount of 250 mg was packed in a
129
tubular U-shaped quartz cell, preheated at 500 ºC with a heating rate of 10 ºC/min
130
in a He flow (50 mL/min) for 110 min to eliminate physisorbed species and
131
cooled to 70 ºC. Then a constant flow of 30 mL/min of 5 vol. % NH3/Ar gas
132
mixture was introduced over the samples for 30 min to achieve saturation. After
133
purging with He for 5 min to remove physisorbed NH3, then, the sample was
134
heated to 130 ºC with a heating rate of 10 ºC/min and held for 3 h to remove
135
physisorbed species. The NH3-TPD measurement was performed from 130 to 850
136
ºC with a heating rate of 10 ºC/min with He as a carrier gas. The number of acid
137
sites was calculated from the peak area compared to a reference material with a
138
known number of acid sites (ZSM-5) that was analyzed with the same conditions.
139
140
Results and discussion
141
The XRD pattern of the obtained products from refluxed rice husk silica
142
including R-MOR-30, R-MOR-50 and R-MOR-70 are illustrated in Figure 1. The
143
pattern of all samples contained peaks with similar positions to those of NaMOR
144
reported in literatures (Kulawong et al., 2011; Zhang et al., 2009, Mignoni et al.,
145
2008). The order of relative peak intensity changed when the gel volume. From R-
146
MOR-30 the strongest peak was 9.8º followed by 25.7º corresponding to the plane
147
200 and 202, respectively. From R-MOR-50 the order of relative intensity was
148
similar but the second peak became stronger. From R-MOR-70 a switch in the
149
intensity order was observed. The growth of zeolite crystal depends on solubility
150
of the starting material and equilibrium within the autoclave during
151
crystallization. The larger volume of the gel led to the higher autogeneous
152
pressure in the autoclave and resulted in higher solubility of the starting material.
153
The crystal growth in the 202 plane for from reflux RHS increased with the gel
154
volume. Kulawong et al. (2011) reported that NaMOR synthesized with a 150 mL
155
capacity autoclave showed the strongest XRD peak at 25.6º. When the synthesis
156
was done with a 150 mL capacity autoclave, the peak at 9.8º became a dominant
157
one.
158
The XRD pattern of the obtained products from precipitated rice husk
159
silica including P-MOR-30, P-MOR-50 and P-MOR-70 are illustrated in Figure 2.
160
The patterns of all samples also contain characteristic peaks of NaMOR
161
(Kulawong et al., 2011; Zhang et al., 2009, M. L. Mignoni et al., 2008) with the
162
strongest peak from the plan 202. The intensity of the plan 200 increased with the
163
gel volume. From P-MOR-50 and P-MOR-70, the intensity of the peak at 6.5º
164
(corresponding to the plane 110) was significantly higher than that from P-MOR-
165
50. The XRD pattern depends on the synthesis conditions. For example, it was
166
reported by Structure Commission of the International Zeolite Association that
167
intensity of the plan 200 was the highest in NaMOR with Si/Al ration of 5
168
(Baerlocher and McCusker, www).
169
The Si/Al ratios of all samples determined by XRF are listed in Table 1.
170
The ratio in the product from both silica sources was higher than that in the gel.
171
The Si/Al ratio of NaMOR from refluxed RHS increased with the gel volume.
172
This result could be from the higher solubility of RHS for the sample with the
173
higher gel volume. In case of NaMOR from precipitated RHS, the change in Si/Al
174
ration could not be related to the gel volume. The lowest Si/Al ratio was from P-
175
MOR-50. From observation the silica from precipitation could be dissolved more
176
easily than the refluxed RHS.
177
The N2 adsorption-desorption isotherm of the NaMOR are presented in
178
Figure 3. The isotherm of all samples was type I which is the characteristic of
179
microporous materials. The adsorption increased rapidly at low relative pressure
180
corresponding to the adsorption in micropores and became nearly constant
181
afterward. The BET surface areas are included in Table 1. The surface area of
182
NaMOR synthesized with refluxed RHS increased with the gel volume. The
183
surface area of R-MOR-30 was significantly lower than R-MOR-50 and R-MOR-
184
70 implying that R-MOR-30 had lower crystallinity. This could be the effect from
185
lower pressure in the autoclave which resulted in the lower solubility of RHS. In
186
contrast, the surface areas of NaMOR prepared from precipitated RHS were
187
similar. This result may due to the higher solubility of RRHS.
188
The NH3-TPD profiles of the NaMOR synthesized with different volumes
189
are shown in Figure 4. Normally, NaMOR exhibited only one peak at low
190
temperature (Katada et al., 2007). All NaMOR from this work also exhibited an
191
additional small peak at high temperature. Similar observation was reported by
192
Kulawong et al. (2011). The peak at low and high temperature corresponded to
193
ammonia desorbed from Brønsted and Lewis acid sites, respectively (Karge and
194
Dondud, 1989; Ma et al., 2000). The intensity of desorption of NaMOR from both
195
silica sources increased with the gel volume. The desorption temperature of R-
196
MOR-70 and P-MOR-70 was lower than that of other samples corresponding to
197
the weaker acid sites. Ma et al. (2000) proposed that the ammonia desorption from
198
ZSM-5 at low temperature associated with the ammonia adsorbed either on Si–
199
OH or from non-zeolitic impurity. The peak desorbed at high temperature was
200
related with the ammonia adsorbed on Si–OH–Al.
201
SEM micrographs of the NaMOR synthesized from refluxed and
202
precipitated RHS are illustrated in Figure 5 and 6, respectively. Particles of
203
NaMOR synthesized from refluxed RHS (Figure 5) were not uniform in size and
204
shape. Aggregated plate-like sheets and amorphous-like matter were observed.
205
Particles of NaMOR synthesized from precipitated RHS (Figure 6) were more
206
uniform with less amorphous-like matter. The particle size decreased with the gel
207
volume in the autoclave. The larger crystal size related to small number of nuclei
208
formation in the synthesis gel (Cubillas and Anderson, 2010; Cundy and Cox,
209
2005). Moreover, the uniform of the zeolite crystal synthesized by using
210
hydrothermal method crucially related to homogeneous distribution of the starting
211
nuclei in the system (Mintova and Valtchev, 2002).
212
213
Conclusions
214
NaMOR was synthesized by hydrothermal method using refluxed and precipitated
215
rice husk silica (RHS). All products gave characteristic XRD peaks of NaMOR
216
with differences in relative intensity.
217
refluxed RHS changed from plane 200 to 202 with the increase of starting gel in
218
the autoclave. On the other hand, the strongest peak in NaMOR from precipitated
219
RHS was from the plan 202. In NaMOR from refluxed RHS the Si/Al ratio,
220
surface area and Brønsted acidity increased with the gel volume. In NaMOR from
221
precipitated RHS the connection between either Si/Al ratio or surface area and the
222
gel volume could not be made, however, the Brønsted acidity increased with the
223
gel volume. The NaMOR from precipitated RHS had higher surface area and
224
uniformity in particle shape and size more than that from refluxed RHS.
225
The strongest peak in NaMOR from
226
Acknowledgements
227
Scholarship for S. Rakmae was from Royal Golden Jubilee Ph.D. program from
228
Thailand Research Fund (TRF) and Suranaree University of Technology (Grant
229
No. PHD/0173/2553).
230
231
References
232
Artkla, S., Grisdanurak, N., Neramittagapong, S., and Wittayakun, J. (2008).
233
Characterization and catalytic performance on transesterification of palm olein
234
of potassium oxide supported on RH-MCM-41 from rice husk silica, Suranaree
235
J. Sci. Technol. 15(2):133-138.
236
237
Baerlocher, Ch. and McCusker, L.B., Database of Zeolite Structures:
http://www.iza-structure.org/databases/
238
Cubillas, P., and Anderson, M.W. (2010). Pore structure, diffusion and activity at
239
the subcrystal level. In: Zeolites and catalysis. Cejka, J., Corma, A., and Zones,
240
S., (eds). Wiley-VCH, Weinheim, p. 375-379.
241
Cundy, C.S. and Cox, P.A. (2005). The hydrothermal synthesis of zeolites:
242
Precursors, intermediates and reaction mechanism. Micropor. Mesopor. Mater.
243
82(1-2):1-78.
244
245
246
247
Juliano, B.O., Maniñgat, C.C., and Pascual, C.G. (1987). Properties of fraction of
rice hull. Phytochemistry. 26(12):3261-3263.
Kalapathy, U., Proctor, A., and Shultz, J. (2000). A simple method for production
of pure silica from rice hull ash. Biores. Technol. 73(3):257-262.
248
Karge , H.G. and Dondur, V. (1990). Investigation of the distribution of acidity in
249
zeolites by temperature-programmed desorption of probe molecules. I.
250
Dealuminated. J. Phys. Chem. 94 (2):765-772.
251
Katada, N., Kanai, T., and Niwa, M. (2004). Dealumination of proton form
252
mordenite with high aluminum content in atmosphere. Micropor. Mesopor.
253
Mater.75(1-2): 61-67.
254
Khabuanchalad, S. Khemthong, P., Prayoonpokarach, S., and Wittayakun, J.
255
(2008). Transformation of zeolite NaY synthesized from rice husk silica to NaP
256
during hydrothermal synthesis, Suranaree J. Sci. Technol. 15(3):225-231.
257
Khemthong, P., Prayoonpokarach, S., and Wittayakun, J. (2007). Synthesis and
258
characterization of zeolite LSX from rice husk silica, Suranaree J. Sci.
259
Technol. 14(4):367-379.
260
261
Kim, G.J. and Ahn, W.S. (1991) Direct synthesis and characterization of highSiO2-content mordenites, Zeolites, 11(7):745-750.
262
Kordatos, K., Gavela, S., Ntziouni, A., Pistiolas, K.N., Kyritsi, A., and
263
Kasselouri-Rigopoulou V. (2008). Synthesis of highly siliceous ZSM-5 zeolite
264
using silica from rice husk ash. Micropor. Mesopor. Mater.115(1-2):189-196.
265
Krishnarao, R.V., Subrahmanyam, J., and Kumar, T.J. (2001). Studies on the
266
formation of black particles in rice husk silica ash. J. Eur. Ceram. Soc.
267
21(1):99-104.
268
Kulawong, S., Prayoonpokaracha, S., Neramittagapong, A., and Wittayakun, J.
269
(2011). Mordenite modification and utililization as supports for iron catalyst
270
for phenol hydroxylation Journal of Industrial and Engineering Chemistry,
271
17(2): 346-351.
272
273
Liou, T.H. (2004). Preparation and characterization of nano-structured silica from
rice husk. Mater. Sci. Eng. A. 364(1-2):313-323.
274
Liou, T.H. and Yang, C.C. (2011). Synthesis and surface characteristics of
275
nanosilica produced from alkali-extracted rice husk ash. Mater. Sci. Eng. B.
276
176(7):521-529.
277
Loiha, S., Föttinger, K., Zorn, K., Klysubun, W., Rupprechter, G., and
278
Wittayakun, J. (2009). Catalytic enhancement of platinum supported on zeolite
279
beta for toluene hydrogenation by addition of palladium, J. Ind. Eng. Chem., 15
280
(6):819-823.
281
Ma, D., Zhang, W., Shu, Y., Liu, X., Xu, Y., and Bao, X. (2000). MAS NMR,
282
ESR and TPD studies of Mo/HZSM-5 catalysts: evidence for the migration of
283
molybdenum species into the zeolitic channels. Catal. Lett. 66(3):155-160.
284
Makornpan, M., Mongkolkachit, C., and Wasanapiarnpong, T. (2013). Fabrication
285
of silicon carbide ceramics from rice husks, Suranaree J. Sci. Technol.
286
21(2):79-86.
287
Mao, R.L.V., Al-Yassir, N., Lu, L., Vu, N.T., and Fortier, A. (2006). New
288
method for the study of surface acidity of zeolites by NH3-TPD, using a pH-
289
meter equipped with an ion selective electrode. Catal. Lett. 112(1–2):13-18.
290
Meier, W. M. (1961). The crystal structure of mordenite (ptilolite), Z. Kristallogr.
291
115:439-450.
292
Mignoni, M.L., Petkowicz, D.I., Machado, N.R.C.F., and Pergher, S.B.C. (2008).
293
Synthesis of mordenite using kaolin as Si and Al source. Appl. Clay Sci. 41(1-
294
2):99-104.
295
Mintova, S., and Valtchev, V. (2002). Effect of the silica source on the formation
296
of nanosized silicalite-1: an in situ dynamic light scattering study. Micropor.
297
Mesopor. Mater. 55(2):171-179.
298
Naskar, M.K., Kundu, D., and Chatterjee, M. (2012). A Facile Hydrothermal
299
Conversion of Rice Husk Ash to ZSM-5 Zeolite Powders. J. Am. Ceram. Soc.
300
95(3):925-930.
301
302
303
Panpa, W. and Jinawath, S. (2009). Synthesis of ZSM-5 zeolite and silicalite
from rice husk ash. Applied Catal. B: Environ., 90(3-4):389-394.
Pimsuta, M., Neramittagapong, A., Prayoonpokarach, S. and Wittayakun, J.
304
(2012) Desilication of NaZSM-5 and Utilization as Support of Fe for Phenol
305
Hydroxylation. Inter. J. Chem. Eng. Appl., 3(2):86-91.
306
Pantu, P., Boekfa, B., and Limtrakul, J. (2007). The adsorption of saturated and
307
unsaturated hydrocarbons on nanostructured zeolites (H-MOR and H-FAU):
308
An ONIOM study, J. Mol. Catal. A-Chem. 277(1-2): 171-179.
309
Roland, E. and Kleinschmit, P., Zeolites; in Bohnet, M; Brinker, C. J., eds.;
310
Ullmann’s Encyclopedia of Industrial Chemistry, 6th ed., Wiley: Weinheim,
311
2003.
312
Tepamat, T., Mongkolkachit, C., and Wasanapiarnpong, T. (2013). Synthesis of
313
zeolite NaA and activated carbon composite from rice husk. Suranaree J. Sci.
314
Technol. 21(2):119-123.
315
Wittayakun, J., Khemthong, P., and Prayoonpokarach, S. (2008). Synthesis and
316
characterization of zeolite NaY from rice husk silica. Korean J. Chem. Eng., 25
317
(4):861-864.
318
Zhang, L., Laak, A.N.C., Jongh, P.E., and Jong, K.P. (2009). Synthesis of large
319
mordenite crystals with different aspect ratios. Micropor. Mesopor. Mater.
320
126(1-2):115-124.
321
322
Table 1: Si/Al ratio and surface area of the synthesized MOR
323
% Gel
volume in
autoclave
30
Gel
Si/Al
Product
Si/Al
BET surface
area (m2/g)
R-MOR-30
Method to
obtain rice
husk silica
Reflux
14.6
57.6
215
R-MOR-50
Reflux
50
14.6
62.2
357
R-MOR-70
Reflux
70
14.6
65.2
347
P-MOR-30
Precipitation
30
14.6
56.1
435
P-MOR-50
Precipitation
50
14.6
48.1
432
P-MOR-70
Precipitation
70
14.6
49.3
418
Sample
324
325
326
327
328
Figure 1 XRD patterns of NaMOR synthesized from rice husk silica from reflux
329
with volume 30, 50 and 70% of the autoclave
330
331
332
333
Figure 2 XRD patterns of NaMOR synthesized from precipitated rice husk silica
334
with volume 30, 50 and 70% of the autoclave
335
336
337
338
339
Figure 3. N2 adsorption–desorption isotherm of NaMOR synthesized with various
volumes by using (a) RRHS and (b) PRHS.
340
341
342
343
344
345
346
347
348
349
350
351
352
353
354
355
356
357
358
359
360
Figure 4 NH3-TPD spectra of NaMOR with different starting material volume;
361
(a) synthesized from R-RHS and (b) synthesized from P-RHS
362
363
364
365
366
367
368
369
370
371
372
373
374
375
376
377
378
379
380
Figure 5 SEM images of NaMOR zeolites synthesized from R-RHS (a) R-MOR-
381
30 (low magnification) (b) R-MOR-30 (high magnification) (c) R-
382
MOR-50 (low magnification) (d) R-MOR-50 (high magnification) (e)
383
R-MOR-70 (low magnification) (f) R-MOR-70 (high magnification)
384
385
386
387
388
389
390
391
392
393
394
395
396
397
398
399
400
401
402
403
Figure 6 SEM images of NaMOR zeolites synthesized from PRHS (a) P-MOR-
404
30 (low magnification) (b) P-MOR-30 (high magnification) (c) P-
405
MOR-50 (low magnification) (d) P-MOR-50 (high magnification) (e)
406
P-MOR-70 (low magnification) (f) P-MOR-70 (high magnification)
Download