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C. Mahender et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213

RESEARCH ARTICLE

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OPEN ACCESS

Synthesis of Nano Phase Titanium Dioxide (Tio2) In Diffusion
Flame Reactor and It Application in Photocatalytic Reaction
C. Mahender*, B. Murali* Dr. V. Himabindu*
*(Centre for Environment, Institute of Science and Technology, Jawaharlal Nehru Technological University
Hyderabad, Kukatpally, Hyderabad-500 085, A.P, India)

ABSTRACT
Nano phase Titanium dioxide (TiO2) is synthesized by flame synthesis method using LPG as fuel, oxygen as
oxidant. In this method Titanium Tetraisopropoxide (TTIP) is used as titanium. The synthesized Nano phase
TiO2 is characterized by SEM and XRD. In this current paper process parameters has been investigated to
synthesize the Nano-phase TiO2 in Flame reactor and its performance is studied in photocatalytic reaction. The
performance of the synthesized Nano-phase TiO2 is compared with Degussa P25 catalyst. The results conclude
that Nano-phase TiO2 shows better performance then Degussa P25.
Keywords - Flame synthesis, LPG, Nano rods, Nano TiO2, Titanium tetraisopropoxide

1

INTRODUCTION

Gas phase combustion synthesis of
inorganic particles is used routinely today to make a
variety of commodities like SiO2, TiO2, Al2O3 etc.
Titanium dioxide (TiO2) is a wide-band gap (3.2eV)
semiconductor; it is one of many metal oxides
currently under investigation. It is readily converted
into different nanostructured forms, including
nanotubes.TiO2 has attracted considerable attention
because it has great potential applications such as
catalysis [1], Photocatalysis [2] and dye-sensitized
solar cells [3] extensive research has been conducted
on TiO2 nanoparticles [4] thin film [5] and
mesoporous TiO2 [6, 7].The two mainstream methods
to synthesize nano-particles are wet methods (sol-gel)
and aerosol methods such as flame synthesis. Wet
methods offer fine control over particle size and
particle size distributions. However in wet- process
the final product often includes a mixture of
amorphous and crystalline particles, resulting in
costly and time consuming in post process steps.
Flame aerosol methods can be operated continuously
allowing for greater output with minimal post
processing. Recently much research has be done to
obtain TiO2 nanotubes with a large surface area and
high photocatalytic activity. P. Hoyer et al
synthesized
TiO2 nano tubes with diameter of 70-100 nm
with sol-gel method [8].H. Imai 1n 1996 reported
anatase phase TiO2 nanotubes with diameter of 8nm
[9].anatase and rutiles phase TiO2 nanotubes has been
synthesized by S.L. Zang group in 2000 [10]. Kranthi
K. Akurati [11] synthesized TiO2 nanoparticles by
Flame aerosol method using methane, Oxygen as fuel
and
oxidant
respectively
with
Titanium
tetraisopropoxide as precursor. Ashok Bhanwala et al
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[12] synthesized pure and carbon doped TiO2
nanoparticles in flame aerosol reactor using
inexpensive fuel gas LPG (liquid petroleum gas) as
fuel and air/Oxygen as oxidant with titanium
tetrachloride (TiCl4) as precursor, reported using of
oxygen instead of air increases the production of
spherical particles with average diameter of particle
size is 104nm. Jaturong Jitputti and his group [13]
proved that TiO2 nanotubes synthesized by
hydrothermal treatment of Degussa P-25 showed
higher photocatalytic activity then Degussa P-25
commercially available. These methods produce
fewer byproducts, usually making them more
economically viable then wet methods [14, 15].
In this current paper Nano-phase TiO2 is
synthesized by diffusion Flame reactor using LPG as
fuel and oxygen as oxidant. The performance of the
flame synthesized nano phase TiO2 is compared with
Degussa P25 catalyst in photocatalysis reaction to
degrade the amount methylene.

2. Materials and methods
2.1. Materials
Titanium tetraisopropoxide (TTIP) are
purchased from SRL Chemicals India, LPG
(domestic, Bharat Gas), oxygen and Nitrogen gas is
purchased from Industrial gas Aagency of Pvt. Ltd
India. All Experiments carried out in a Flame reactor
indigenously by JNTUH Hyderabad as shown in Fig1.
2.2 Methodology
The flame reactor has been indigenously designed
to produce nano materials. The detailed setup of the
reactor has been discussed in our previous paper to
synthesis of nano carbon materials. [16] The reactor
209 | P a g e
C. Mahender et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213
operates under atmospheric pressure. The measured
quantity of the LPG and the oxidant reaches the
ignition chamber. During the process we have
observed the dark orange flame color which is
perfectly in a spindle form. Along the entire length of
the flame, its temperature was recorded using a Ktype thermocouple.
In this study, Nano-phase TiO2 were
synthesized in diffusion flame by using titanium
tetraisoproxide (TTIP, 98% purity, spectrochem) as
the titanium precursor. In this Experiment Flame is
ignited in the burner with LPG and Oxygen, Nitrogen
gas is bubbled through a Reagent vessel containing
liquid TTIP to deliver the TTIP vapour to the burner,
as shown in Fig-2.In order to prevent any
condensation of the precursor, all gas line
downstream the TTIP reagent vessel and the burner
were wrapped with heating tapes to maintain them at
125oC.The TiO2 produced is captured on a glass fiber
filter (Axiva GF/A) Fig-3, is scrapped carefully and
weighed. Later heat treated at 350 OC in the presence
of air for 60 minutes to remove any traces of
amorphous carbon impurities then the samples were
characterized by SEM and XRD.

3.0 Characterization
3.1 X-ray Diffraction Analysis
The XRD ( 7000 Schimazu) analysis was
carried out using Cu K1 type of radiation with a
wavelength () of 1.54060 Ao. XRD graph of TiO2
nano materials produced using LPG-Oxygen at flow
rates of 0.2Slpm and 0.7 Slpm is shown in Fig-4. The
step size was 0.02 degree/step and step time was 0.2
sec/step. The working range was 2ɵ = 20-100, the
average crystal size TiO2 is calculated according the
equation (1) is commonly known as scherer’s
equation [17] by selecting particle peak
(suryanarayana and Norton, 1998).

Where L is the length of the crystal in the direction of
the d spacing, K is the constant of 0.9, ɵ is the
wavelength of X-Ray,β is the full width at halfmaximum (FWHM) of the selected peak and ɵ is the
Bragg’s angle of the diffraction of the peak. The
mass fraction of the Anatase and Rutile phase content
is calculated by intensities of the XRD spectra
according to spurr’s equation [18] shown in equation
(2)

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Where Fr is the percentage content of rutile, IA (101)
and IR (110) are the integral intensities of (101) of
Anatase and (110) of Rutile, respectively.
3.2 Scanning Electron Microscope (SEM) Analysis
The samples were analyzed using Phillips
XL 30 series Scanning Electron Microscope (SEM)
in Osmania University college of Technology,
Hyderabad. From the Fig-6 we can see a dense
growth of TiO2 particles synthesized by using
diffusion reactor using LPG and Oxygen at a Flow
rate of 0.2 Slpm and 0.7 Slpm respectively. Where as
in Fig-7 we can observe SEM image of Degussa P25
TiO2 catalyst similarly equal to our flame synthesized
Nano phase TiO2.

4.0 Results and Discussion
Nano phase Titanium Dioxide
is
successfully synthesized by using a pilot Scale
Diffusion Flame reactor, using inexpensive fuel, LPG
as fuel and Oxygen as oxidant.Fig-4 and Fig-6 is the
XRD pattern and SEM image of the TiO2 material
synthesized at flowrate of 0.2 and 0.7 Slpm of LPG
and Oxygen. Using PCPDFWIN –XRD database the
peaks were identified for their lattice structure of the
orientation. The strongest peaks of TiO2 (Fig-4)
corresponds at 2ɵ = 25.323 is Anatase (101) and at
2ɵ = 27.421 is Rutile (110).The average particle
diameter (equation-1) is calculated from scherer’s at
2ɵ of 25.32 is 26 nm. Anatase and Rutile content is
calculated from equation-2 is 65% Anatase and 28%
Rutile. Fig-5 and Fig-7 are the XRD pattern and SEM
images of the Degussa P25 catalyst anatase phase of
P25 is 80% and rutile phase is 20%. As compared to
Degussa P25 catalyst flame synthesized nano catalyst
contain less amount of anatase phase but average
particle diameter of P25 is 43nm which is higher then
flame synthesized catalyst.
4.1 Photocatalytic performance of catalysts
Performance of the combustion method
synthesized TiO2 (C-TiO2) has been tested in a UV
photocatalytic reaction to degrade the methylene blue
compound for about 3 hours duration at neutral pH
(7.0) condition. The results reveal that P25 has
degraded the MB from 20 to 8 ppm whereas C-TiO2
is from 20 to 2.2ppm with in 3hours time the
degradation graph as shown in Fig-8. C-TiO2 is 15%
more efficient then P25.Even though the p25 has
more anatase phase (Anatase content 80%) then CTiO2 (Anatase content 65%) calculated from
Equation – (2). Synthesized C-TiO2 showed more
efficient then P25.

5.0 Conclusion
A pilot scale Diffusion flame reactor
experiments has been carried out to synthesis the
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210 | P a g e
C. Mahender et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213
Nano C- TiO2 materials, with inexpensive LPG as
fuel gas, Oxygen as oxidant in flame reactor. In this
experiment TTIP is used as Precursor for TiO2
material and nitrogen as carrier gas. C-TiO2 is
synthesized with LPG flowrate of 0.2 slpm and
0.7slpm of oxygen contain 65% of anatase and 28 %
of rutile phase showed better performance than p25
even though it had 80% anatase content. The
synthesized C-TiO2 has average particle diameter of
26nm, calculated from XRD data scherer equation
where as P25 has 46nm.Hence in this paper one step
synthesis method of Nano phase TiO2 method is
described using LPG as fuel and oxygen as Oxidant
in flame reactor. This one step synthesis method is
very useful compared to sol-Gel method where
requires numbers of synthesis steps like filteration,
purification and calcination in sol-gel method.

[13]

[14]
[15]
[16]

[17]

[18]

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Jaturong Jitputti, Sorapang Pavasupree,
Yoshikazu Suzuki and Susumu Yoshikawa,
Japanese J.Appl.Phys Vol .47, No.1, 2008,
pp. 751-756.
S.E. Pratsinis, S.Vemury, powder Technol,
88 (1996) 267-273.
S.E. Pratsinis, prog. Energy combust.Sci. 24
(1998) 197-219.
Vivek Dhand, J.S Prasad, M. Venkateswara
Rao, K. Naga Mahesh, L. Anupama, Hima
bindu, Anjaneyulu Yerramilli, V.S. Raju,
A.A. Sukumar Indian journal of Engg &
Mat.Sci Vol. 14, June 2007, pp.235-239.
Suryanarayana, C and M.G Norton, 1998.
X-Ray Diffraction a practical approach.New
York, plenum press.
Spurr,
R.A,
and
H.
Myers,1957.
Anal.chem.,29 760-762.

Acknowledgements
The authors acknowledge the financial
support given by Defence Research Development
Organization (DRDO), Ministry of Defence, and
Government of India as sponsored R&D project
under which this work is carried out; we thank
Osmania University, College of Technology
Hyderabad for providing SEM and XRD data of all
samples

References
[1]
[2]
[3]
[4]
[5]
[6]
[7]
[8]
[9]

[10]

[11]

[12]

K.I. Hadjiivanov, D.G. Klissurski, Chem.
Soc. Rev. 25 (1996) 61.
A.L. Linsebigler, G. Lu, J.T. Yates, Chem.
Rev. 95 (1995) 735.
B. O.Regan, M. Gratzel, Nature (London)
353 (1991) 737.
W. Chen-Chi, J.Y. Ying, Chem. Mater.
11(1999) 3113.
N. Negishi, K. Takeuchi, T. Ibusuki, J.
Mater. Sci. Lett. 18 (1999) 515.
N. Ulagappan, C.N.R. Rao, Chem.
Commun. (Cambridge) 14 (1996) 1685.
J.S. Yin, Z.L. Wang, Adv. Mater. 11 (1999)
469.
P. Hoyer, Langmuir 12 (1996) 1411.
H. Imai, Y. Takei, K. Shimizu, M. Matsuda,
H. Hirashima, J. Mater. Chem. 9 (1999)
2971.
S.L. Zhang, J.F. Zhou, Z.J. Zhang, Z.L. Du,
A.V. Vorontsov, Z.S. Jin, Chin. Sci. Bull. 45
(2000) 1533.
Kranthi K. Akurati, Andri Vital, Ulrich E.
Klotz, Bastian Bommer, Thomas Graule,
Markus Winterer, powder Technol.165
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Ashok Kumar Bhanwala, Ashok Kumar,
D.P.Mishra, Jitendra Kumar, J. Aerosol. Sci
40 (2009) 720-730.

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Figure Citations:
Figure 1 – Flame Reactor setup, with flow meters
front view (Rotameters).
Figure 2 – Flow chart diagram of flame reactor unit.
Figure 3 –Sample collector with glass fiber filter
paper holder.
Figure 4 – XRD Pattern of Flame synthesized TiO2 at
0.2 Slpm.
Figure 5- XRD Pattern of Flame synthesized P25
Figure 6- SEM image of the Flame synthesizes TiO2
Figure 7- SEM image of P25
Figure 8- Photocatalytic acitivity of the P25 and CTiO2

Figures

Figure 1 – Flame Reactor setup, with flow meters
front view (Rotameters).

211 | P a g e
C. Mahender et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213

www.ijera.com

Figure 2 – Flow chart diagram of flame reactor unit
Figure 5- XRD Pattern of Flame synthesized P25

Figure 3 –Sample collector with glass fiber filter
paper holder.
Figure 6- SEM image of the Flame synthesizes TiO2

Figure 4 – XRD Pattern of Flame synthesized TiO2 at
0.2 Slpm.

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Figure 7- SEM image of P25

212 | P a g e
C. Mahender et al Int. Journal of Engineering Research and Applications
ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213

www.ijera.com

Figure 8- Photocatalytic acitivity of the P25 and CTiO2

www.ijera.com

213 | P a g e

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Ae4201209213

  • 1. C. Mahender et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213 RESEARCH ARTICLE www.ijera.com OPEN ACCESS Synthesis of Nano Phase Titanium Dioxide (Tio2) In Diffusion Flame Reactor and It Application in Photocatalytic Reaction C. Mahender*, B. Murali* Dr. V. Himabindu* *(Centre for Environment, Institute of Science and Technology, Jawaharlal Nehru Technological University Hyderabad, Kukatpally, Hyderabad-500 085, A.P, India) ABSTRACT Nano phase Titanium dioxide (TiO2) is synthesized by flame synthesis method using LPG as fuel, oxygen as oxidant. In this method Titanium Tetraisopropoxide (TTIP) is used as titanium. The synthesized Nano phase TiO2 is characterized by SEM and XRD. In this current paper process parameters has been investigated to synthesize the Nano-phase TiO2 in Flame reactor and its performance is studied in photocatalytic reaction. The performance of the synthesized Nano-phase TiO2 is compared with Degussa P25 catalyst. The results conclude that Nano-phase TiO2 shows better performance then Degussa P25. Keywords - Flame synthesis, LPG, Nano rods, Nano TiO2, Titanium tetraisopropoxide 1 INTRODUCTION Gas phase combustion synthesis of inorganic particles is used routinely today to make a variety of commodities like SiO2, TiO2, Al2O3 etc. Titanium dioxide (TiO2) is a wide-band gap (3.2eV) semiconductor; it is one of many metal oxides currently under investigation. It is readily converted into different nanostructured forms, including nanotubes.TiO2 has attracted considerable attention because it has great potential applications such as catalysis [1], Photocatalysis [2] and dye-sensitized solar cells [3] extensive research has been conducted on TiO2 nanoparticles [4] thin film [5] and mesoporous TiO2 [6, 7].The two mainstream methods to synthesize nano-particles are wet methods (sol-gel) and aerosol methods such as flame synthesis. Wet methods offer fine control over particle size and particle size distributions. However in wet- process the final product often includes a mixture of amorphous and crystalline particles, resulting in costly and time consuming in post process steps. Flame aerosol methods can be operated continuously allowing for greater output with minimal post processing. Recently much research has be done to obtain TiO2 nanotubes with a large surface area and high photocatalytic activity. P. Hoyer et al synthesized TiO2 nano tubes with diameter of 70-100 nm with sol-gel method [8].H. Imai 1n 1996 reported anatase phase TiO2 nanotubes with diameter of 8nm [9].anatase and rutiles phase TiO2 nanotubes has been synthesized by S.L. Zang group in 2000 [10]. Kranthi K. Akurati [11] synthesized TiO2 nanoparticles by Flame aerosol method using methane, Oxygen as fuel and oxidant respectively with Titanium tetraisopropoxide as precursor. Ashok Bhanwala et al www.ijera.com [12] synthesized pure and carbon doped TiO2 nanoparticles in flame aerosol reactor using inexpensive fuel gas LPG (liquid petroleum gas) as fuel and air/Oxygen as oxidant with titanium tetrachloride (TiCl4) as precursor, reported using of oxygen instead of air increases the production of spherical particles with average diameter of particle size is 104nm. Jaturong Jitputti and his group [13] proved that TiO2 nanotubes synthesized by hydrothermal treatment of Degussa P-25 showed higher photocatalytic activity then Degussa P-25 commercially available. These methods produce fewer byproducts, usually making them more economically viable then wet methods [14, 15]. In this current paper Nano-phase TiO2 is synthesized by diffusion Flame reactor using LPG as fuel and oxygen as oxidant. The performance of the flame synthesized nano phase TiO2 is compared with Degussa P25 catalyst in photocatalysis reaction to degrade the amount methylene. 2. Materials and methods 2.1. Materials Titanium tetraisopropoxide (TTIP) are purchased from SRL Chemicals India, LPG (domestic, Bharat Gas), oxygen and Nitrogen gas is purchased from Industrial gas Aagency of Pvt. Ltd India. All Experiments carried out in a Flame reactor indigenously by JNTUH Hyderabad as shown in Fig1. 2.2 Methodology The flame reactor has been indigenously designed to produce nano materials. The detailed setup of the reactor has been discussed in our previous paper to synthesis of nano carbon materials. [16] The reactor 209 | P a g e
  • 2. C. Mahender et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213 operates under atmospheric pressure. The measured quantity of the LPG and the oxidant reaches the ignition chamber. During the process we have observed the dark orange flame color which is perfectly in a spindle form. Along the entire length of the flame, its temperature was recorded using a Ktype thermocouple. In this study, Nano-phase TiO2 were synthesized in diffusion flame by using titanium tetraisoproxide (TTIP, 98% purity, spectrochem) as the titanium precursor. In this Experiment Flame is ignited in the burner with LPG and Oxygen, Nitrogen gas is bubbled through a Reagent vessel containing liquid TTIP to deliver the TTIP vapour to the burner, as shown in Fig-2.In order to prevent any condensation of the precursor, all gas line downstream the TTIP reagent vessel and the burner were wrapped with heating tapes to maintain them at 125oC.The TiO2 produced is captured on a glass fiber filter (Axiva GF/A) Fig-3, is scrapped carefully and weighed. Later heat treated at 350 OC in the presence of air for 60 minutes to remove any traces of amorphous carbon impurities then the samples were characterized by SEM and XRD. 3.0 Characterization 3.1 X-ray Diffraction Analysis The XRD ( 7000 Schimazu) analysis was carried out using Cu K1 type of radiation with a wavelength () of 1.54060 Ao. XRD graph of TiO2 nano materials produced using LPG-Oxygen at flow rates of 0.2Slpm and 0.7 Slpm is shown in Fig-4. The step size was 0.02 degree/step and step time was 0.2 sec/step. The working range was 2ɵ = 20-100, the average crystal size TiO2 is calculated according the equation (1) is commonly known as scherer’s equation [17] by selecting particle peak (suryanarayana and Norton, 1998). Where L is the length of the crystal in the direction of the d spacing, K is the constant of 0.9, ɵ is the wavelength of X-Ray,β is the full width at halfmaximum (FWHM) of the selected peak and ɵ is the Bragg’s angle of the diffraction of the peak. The mass fraction of the Anatase and Rutile phase content is calculated by intensities of the XRD spectra according to spurr’s equation [18] shown in equation (2) www.ijera.com Where Fr is the percentage content of rutile, IA (101) and IR (110) are the integral intensities of (101) of Anatase and (110) of Rutile, respectively. 3.2 Scanning Electron Microscope (SEM) Analysis The samples were analyzed using Phillips XL 30 series Scanning Electron Microscope (SEM) in Osmania University college of Technology, Hyderabad. From the Fig-6 we can see a dense growth of TiO2 particles synthesized by using diffusion reactor using LPG and Oxygen at a Flow rate of 0.2 Slpm and 0.7 Slpm respectively. Where as in Fig-7 we can observe SEM image of Degussa P25 TiO2 catalyst similarly equal to our flame synthesized Nano phase TiO2. 4.0 Results and Discussion Nano phase Titanium Dioxide is successfully synthesized by using a pilot Scale Diffusion Flame reactor, using inexpensive fuel, LPG as fuel and Oxygen as oxidant.Fig-4 and Fig-6 is the XRD pattern and SEM image of the TiO2 material synthesized at flowrate of 0.2 and 0.7 Slpm of LPG and Oxygen. Using PCPDFWIN –XRD database the peaks were identified for their lattice structure of the orientation. The strongest peaks of TiO2 (Fig-4) corresponds at 2ɵ = 25.323 is Anatase (101) and at 2ɵ = 27.421 is Rutile (110).The average particle diameter (equation-1) is calculated from scherer’s at 2ɵ of 25.32 is 26 nm. Anatase and Rutile content is calculated from equation-2 is 65% Anatase and 28% Rutile. Fig-5 and Fig-7 are the XRD pattern and SEM images of the Degussa P25 catalyst anatase phase of P25 is 80% and rutile phase is 20%. As compared to Degussa P25 catalyst flame synthesized nano catalyst contain less amount of anatase phase but average particle diameter of P25 is 43nm which is higher then flame synthesized catalyst. 4.1 Photocatalytic performance of catalysts Performance of the combustion method synthesized TiO2 (C-TiO2) has been tested in a UV photocatalytic reaction to degrade the methylene blue compound for about 3 hours duration at neutral pH (7.0) condition. The results reveal that P25 has degraded the MB from 20 to 8 ppm whereas C-TiO2 is from 20 to 2.2ppm with in 3hours time the degradation graph as shown in Fig-8. C-TiO2 is 15% more efficient then P25.Even though the p25 has more anatase phase (Anatase content 80%) then CTiO2 (Anatase content 65%) calculated from Equation – (2). Synthesized C-TiO2 showed more efficient then P25. 5.0 Conclusion A pilot scale Diffusion flame reactor experiments has been carried out to synthesis the www.ijera.com 210 | P a g e
  • 3. C. Mahender et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213 Nano C- TiO2 materials, with inexpensive LPG as fuel gas, Oxygen as oxidant in flame reactor. In this experiment TTIP is used as Precursor for TiO2 material and nitrogen as carrier gas. C-TiO2 is synthesized with LPG flowrate of 0.2 slpm and 0.7slpm of oxygen contain 65% of anatase and 28 % of rutile phase showed better performance than p25 even though it had 80% anatase content. The synthesized C-TiO2 has average particle diameter of 26nm, calculated from XRD data scherer equation where as P25 has 46nm.Hence in this paper one step synthesis method of Nano phase TiO2 method is described using LPG as fuel and oxygen as Oxidant in flame reactor. This one step synthesis method is very useful compared to sol-Gel method where requires numbers of synthesis steps like filteration, purification and calcination in sol-gel method. [13] [14] [15] [16] [17] [18] www.ijera.com Jaturong Jitputti, Sorapang Pavasupree, Yoshikazu Suzuki and Susumu Yoshikawa, Japanese J.Appl.Phys Vol .47, No.1, 2008, pp. 751-756. S.E. Pratsinis, S.Vemury, powder Technol, 88 (1996) 267-273. S.E. Pratsinis, prog. Energy combust.Sci. 24 (1998) 197-219. Vivek Dhand, J.S Prasad, M. Venkateswara Rao, K. Naga Mahesh, L. Anupama, Hima bindu, Anjaneyulu Yerramilli, V.S. Raju, A.A. Sukumar Indian journal of Engg & Mat.Sci Vol. 14, June 2007, pp.235-239. Suryanarayana, C and M.G Norton, 1998. X-Ray Diffraction a practical approach.New York, plenum press. Spurr, R.A, and H. Myers,1957. Anal.chem.,29 760-762. Acknowledgements The authors acknowledge the financial support given by Defence Research Development Organization (DRDO), Ministry of Defence, and Government of India as sponsored R&D project under which this work is carried out; we thank Osmania University, College of Technology Hyderabad for providing SEM and XRD data of all samples References [1] [2] [3] [4] [5] [6] [7] [8] [9] [10] [11] [12] K.I. Hadjiivanov, D.G. Klissurski, Chem. Soc. Rev. 25 (1996) 61. A.L. Linsebigler, G. Lu, J.T. Yates, Chem. Rev. 95 (1995) 735. B. O.Regan, M. Gratzel, Nature (London) 353 (1991) 737. W. Chen-Chi, J.Y. Ying, Chem. Mater. 11(1999) 3113. N. Negishi, K. Takeuchi, T. Ibusuki, J. Mater. Sci. Lett. 18 (1999) 515. N. Ulagappan, C.N.R. Rao, Chem. Commun. (Cambridge) 14 (1996) 1685. J.S. Yin, Z.L. Wang, Adv. Mater. 11 (1999) 469. P. Hoyer, Langmuir 12 (1996) 1411. H. Imai, Y. Takei, K. Shimizu, M. Matsuda, H. Hirashima, J. Mater. Chem. 9 (1999) 2971. S.L. Zhang, J.F. Zhou, Z.J. Zhang, Z.L. Du, A.V. Vorontsov, Z.S. Jin, Chin. Sci. Bull. 45 (2000) 1533. Kranthi K. Akurati, Andri Vital, Ulrich E. Klotz, Bastian Bommer, Thomas Graule, Markus Winterer, powder Technol.165 (2006) 73-82. Ashok Kumar Bhanwala, Ashok Kumar, D.P.Mishra, Jitendra Kumar, J. Aerosol. Sci 40 (2009) 720-730. www.ijera.com Figure Citations: Figure 1 – Flame Reactor setup, with flow meters front view (Rotameters). Figure 2 – Flow chart diagram of flame reactor unit. Figure 3 –Sample collector with glass fiber filter paper holder. Figure 4 – XRD Pattern of Flame synthesized TiO2 at 0.2 Slpm. Figure 5- XRD Pattern of Flame synthesized P25 Figure 6- SEM image of the Flame synthesizes TiO2 Figure 7- SEM image of P25 Figure 8- Photocatalytic acitivity of the P25 and CTiO2 Figures Figure 1 – Flame Reactor setup, with flow meters front view (Rotameters). 211 | P a g e
  • 4. C. Mahender et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213 www.ijera.com Figure 2 – Flow chart diagram of flame reactor unit Figure 5- XRD Pattern of Flame synthesized P25 Figure 3 –Sample collector with glass fiber filter paper holder. Figure 6- SEM image of the Flame synthesizes TiO2 Figure 4 – XRD Pattern of Flame synthesized TiO2 at 0.2 Slpm. www.ijera.com Figure 7- SEM image of P25 212 | P a g e
  • 5. C. Mahender et al Int. Journal of Engineering Research and Applications ISSN : 2248-9622, Vol. 4, Issue 2( Version 1), February 2014, pp.209-213 www.ijera.com Figure 8- Photocatalytic acitivity of the P25 and CTiO2 www.ijera.com 213 | P a g e