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(1)

.bz" öڂž >wVöB w÷Ú~ ;ç *B

˂²Áš;ÖÁË'ç

'Î&v ~ã" ~ãöڂž  ’

(2001j 1ú 3¢ 7>, 2001j 7ú 5¢ j)

Morphological Evolution of the Aggregates in the Premixed Flat Flame Aerosol Reactor

Hankwon Chang, Jeungwoo Lee and Hyuksang Chang

Environmental Aerosol Engineering Laboratory,

Department of Environmental Engineering, Yeungnam University, Kyungsan 712-749, Korea (Received 3 January 2001; accepted 5 July 2001)

º £

4

5 TiCl4¢ "Úê z"NêöB ' bî~ z>w³ê Nš¢ šÏ~ {ÖB‚'ž ãÖf >wB‚'ž ãÖö &š

SiO2 5 TiO2 «¶~ ;ç*B";j šš~º ©š  ’~ Ï'š. «¶;ç &V 5 G;j *š 'ÿj»j š Ôf SiCl4~ ãÖ, *¶*ãj šÏš >wVÚ *~ö V¢ SiO2w÷Ú ;W";j &VŽb‚Ž {Öw÷š w÷Ú ; W~ "º V·b‚ ·ÏNj {ž®. >š >wêVræ >w³ê ç>& ¸² Fæ>º TiCl4~ ãÖ TiO2w÷Ú ;W

25 TiO2w÷Ú~ *¿î Nöf 1.23-1.84, 2.81-2.94‚ '' G;> šº *ã Òê Ö"f ¢~‚.  ’öB B–B TiO2 «¶~ 7/‚B~ ‚Ï&Ë Wj –Ò~V *š XRD ªCj >¯‚ Ö", 7z' ‚Wš ¸f anatase Wªš "Wªªš G;>î.

Abstract−Using a premixed flat flame aerosol reactor, the experimental study on the morphological evolution of the aggre- gates was done. With the objectives to understand the morphological process of SiO2 and TiO2 particle that matches to the cases of the reaction-limited aggregation process and the diffusion-limited aggregation process respectively, the difference in chemical reaction rate of SiCl4 and TiCl4 was utilized under given flame temperatures. To evaluate the morphological evolu- tion of the aggregates, the light scattering measurement and electron microscopy coupled with thermophoretic sampling method were used. In the case of SiCl4 oxidation that produces SiO2 particles, the microscopic observation obtained with respect to the axial position in the reactor showed that the diffusion-limited aggregation was the dominant mechanism in the aggregation process because that the very low reaction rates was maintained excepted the earlier reaction stage in the given reactor temperature profile. In the case of TiCl4 that maintains the higher reaction rate during the later reaction stage, it was observed that the reaction-limited aggregation process is the main mechanism on the aggregation. According to the results of the light scattering measurements, the fractal dimension of SiO2 and TiO2 aggregates was 1.23-1.84 and 2.81-2.94 respec- tively, and those results are corresponds with the photometric measurement. To observe applicability of TiO2 particles as pho- tocatalyst, XRD analysis was conducted. TiO2 particles were generated in our study consisted of anatase mainly that has high photochemical activity.

Key words: Morphology, Aggregation, Light Scattering, Chemical Reaction Rate, Diffusion-limited, Reaction-limited

1. B †

z"ö ~‚ ªÚ W ;f Öë*Ë OšöB Bê bî~

B–¾ βÒ~ B–f ?f çë' ¦&&~¢ <º ªÚ W

;öB 6Ò ÒÏ>Ú æ ®. 7RF B–, >êÚ >N Ëçj

*‚ .^ «¶~ B–, b¦~ b" Oïj *‚ .ã¶ 6º  ã¶~ w÷ڞ Wïnò 5 Oïnò~ ÒϚ j>'ž zË®~ B

–, ‚š'~ &z¢ šÏ‚ 7/, ò*æ 5 &ÊbBf ?f V ËÒò‚B 6Ò šÏ> ®. š‚ çë' ¦&&~ ªÚ~  WöB w÷Ú~ ’V, ’– 6º ‚š'" ?f ’–'ž ßûš ‚

To whom correspondence should be addressed.

E-mail: [email protected]

(2)

z B39² B5^ 2001j 10ú

.b ïš z"[1-5]" &Ë~ {Öz"[6-8]" ?f ’–& *~

Jæj BzÊ z"–š –.~ ϚW r^š. z"" ?f

N ª*VöBº «¶~ 7Ö¦j šÏ‚ j7/ «¶ G;»š ô

š ÒÏ>Úæ ®[1-7, 9-11]. šº FÿËj v¦Êæ p «¶

~ ßWj G;† > ®º Ë6j < ®. 7Ö¦»öº ÿ' 7Ö¦

»(DLS; dynamic light scattering)[7, 9]" ;' 7Ö¦»(SLS; static light scattering)[1, 2, 9-11]š "‚ šÏ> ®. ÿ' 7Ö¦»f «¶~ { ֚ÿ ßWj šÏ‚ «ã G;»š ;' 7Ö¦»f 'êö Vž

Ö¦ßWj šÏ~ «ã ª[1, 2, 10] 5 «¶~ ;ç[2, 9-11]j G

;~º O»š. ÿ' 7Ö¦»~ ãÖöº «¶~ 7 š.†" ? f «¶~ 7 ßWj ræ ášê «ãj G;† > ®b¾, «¶~

;çö &šBº G;~V Ú[. >š ;' 7Ö¦»f «¶~ 7

' ßWš º’>æò, «ã ª 5 «¶~ ;çj G;† > ®Ú «

¶ ;çö &‚ ’öB ôš ÒÏ> ®. Ò «¶ ;çj ç 7'b‚ &V† > ®º *¶*ãj šÏ‚ «¶ ;çö &‚ ’

& ôš šÚæ ®æò, «¶~ ;çj 2Nö šö R'B Ö"

ò áj > ®Ú 3Nö*öB~ «¶ ;çö &‚ ’¢ *šBº 2Nö ;çj 3Nö ;çb‚ ;~º ’& º’>Ú šö &‚ 

«¶~ w÷Ú ;W ";j .G‚ Ξ‚º ª~ V(random

walking)[12-14]f ?f Ûê' O»j šÏ~ «¶~ {ÖÚÿj Î

Ò~  Ö" w÷Ú& ¶V FÒW(self-similarity)j <º *¿î (fractal) ’–~ w÷Ú¢ ;W~º Ξ" >wbî~ z>wö Vž

«¶~ w»j Î҂ Κ BB>Ú ÒÏ>Ú æ ®[15].

 ’öBº ¦&&~ ^ ªö~ &ï B–¢ *‚ Ö Ö>

‚ O»ž z" öڂž >wV¢ ÒÏ~[1, 2], 7Ö¦»" *¶*

>Ú &º ";j Ûê'ž O»j šÏ~ *ÖÎÒ Žb‚Ž >w B‚'(reaction limited)ž ãÖf {ÖB‚(diffusion limited)'ž ãÖ

öB WF w÷Ú~ ηj .G~ þ'b‚ G;B Ö"f j v~&.

š‚ ’Ö"f çëÏ ªÚ Wö wÏF > ®j ©b‚  'B. ß®, TiO2«¶f ?f 7/ Òò Öö ®ÚB j‚š' B.

2. š †

w÷Ú ;Wf z>wj ۚ >wzbîš "Úê >wNêö B >w³êç>ö V¢ Wzbî ÃV& WNb‚¦V ·B . zbî~ >w³êf &~ Fig. 1ö º£ J«‚ ©¾" w÷

Ú~ W";f ’² v &æ‚ ¾2 > ®º–, Fig. 1~ 禺 z

>wš æ³'b‚ šÚ^ ‚« «¶~ ;Wö >wš æV'ž ' Ëj ~º ãÖ, ¯ >wB‚' w÷Ú W";" ‚« w÷Ú~ ; çj êz‚ ©š, ~¦º z>wj ۂ Wb ÃV& «¶  W .Vö ‚'b‚ W>Ú w÷Ú~ ;W";ö z>wº

«¶~ {ÖÏòš æV'b‚ 'Ëj ~º ãÖ, ¯ {ÖB‚' w

÷Ú ;W";" ‚« WB w÷Ú~ ;çj ¾æÚî. >w³ê&

.Vöò ‚'b‚ †ž ãÖöº >wbV Wb ÃV& .

b‚Ž î›;W(homogeneous nucleation)š šÚæ, š‚ ž~

 V«¶¢ WŽb‚Ž w÷Ú~ ;Wš ·B. ;WB V«

¶f "Úê žK~ ·Ï ~öB 2¢ÚÚÿ(brownian motion)j Û

š B‚ Ïò~ w÷Ú¢ ;W~V *š B‚ ¢¿º j&'ž

bÒ*ç, ¯ w÷(coagulation)*çj ÐbšB ‚«'b‚ *¿î (fractal) ’–~ w÷Ú& ;WB. >š, >wb‚¦V Wb‚~ z

>wš æ³'b‚ šÚî ãÖöº V«¶~ ›;Wš šÚ ê šêöê ê³'b‚ >wbV Wb~ ÃV& æ³'b‚

¢ W~Vº Vš~ V«¶~ ‚šö ¿Ú «¶~ ‚šj W ËÚb‚Ž «¶~ ’V¢ Ã&ʺ, ¯ w»(condensation) *çj

Fig. 1. Description of aggregation process according to reaction-limited and diffusion-limited model.

(3)

¢bB ‚«'b‚ ’;~ – «¶¢ WÎ.

æ.ræ~ ’[3, 5, 12, 13]öBº ‚« «¶~ ;çj Æ&‚ «¶

~ ;çš ’;š >îj ãÖöº ²Ö(sintering)*çš w÷Ú~ ; çj Ö;~º "º V·b‚ J«>îæò,  ’öBº Nꪾ

>wbî~ ³ê ö ~š 'Ëj Aº >w³ê& «¶~ ;çö "

º 'Ëö &š J«>î.

Fig. 1ö J«‚ š‚ v &æ öڂž~ ;W";j Ξz‚ © 7 &‚'ž ©b‚º Edenö ~š BBB «¶~ ‚šj WËʺ

>wB‚' Ξ(RLA; reaction-limited aggregation model)[15]" «¶

¢ ß; * nö ª~ªB ' «¶¢ 2¢ÚÚÿj Î҂ Š

Úÿj B «¶¢ B‚ Ïò WËʺ {ÖB‚' Ξ(DLA; diffusion- limited aggregation model)š ®[14, 15].

2-1. w÷Ú Îž

>w æV' Ξ~ &‚'ž Ξ‚º Edenš BB‚ Κ[15].

ö6ö seed «¶¢ v seed «¶ "*ö «¶j ~¾O ¦OB

& ¦OF {†š ÿ¢~êƒ FæB. š-² W˂ w÷Ú~ η

f Fig. 2(a)öB ¾æÞ ©" ?š w÷Ú~ ηf &÷B ’–¢ <

º. š‚ Κ <º bÒ' ~º >w&ʂ¦V Wb &Ê

‚ *~ æ³'b‚ šÚ^ Wb~ ÃV(vapor)& >wbV æ³'b‚ W>Ú «¶~ W˚ w÷º «¶‚šö ÃV~ ¦ Oö ~‚ WË ¯, w»š æV'ž ãÖ¢ Î҂ ãÖ¢ † > ® . Fig. 2(a)º 3Nö~ Eden Ξö ~‚ w÷Ú ‚«;çj ¾æÞ © b‚ *¿î Nöf *Nö" ?f 3.0 8j ¾æÚî. šº Eden Ξö ~š WB w÷Ú~ ’–º âöB :f ?š Ö &÷

«¶~ WËöº «¶f «¶*~ Ïòö ~‚ W˚¢Vº V&

WF ©š.

>wB‚' w÷Ú Îžö >š {ÖB‚' w÷Ú Îžf .Vö ß

ª~ V ÚÿÚb‚Ž * nö ®º «¶~ ç^Ïò‚ ž‚

w÷Ú~ ;Wj Î҂[14, 15]. š ";j –öB .V 1,000B~

«¶‚ >¯B DLA Ξ~ ‚« 3Nö ;çj Fig. 2(b)ö ¾æÚî.

š «¶~ *¿î Nöf 3.0ž Eden Ξ"º Ò 1.74¢ ¾æî.

šº ‚šWËö ~‚ w÷Ú~ ;Wb‚ šÚê Ö &÷B ’–

~ w÷Úfº Ò «¶~ {ÖÏòö ~‚ w÷Ú~ ‚« ;çf Ö ®'ššB w÷Ú¢ ’W~ ®º V«¶~ >&êê Ö Ôf ÒҒ–~ ;çš Nj r > ®.

2-2. z>w

 ’öB z"NêöB z>w³ê& ž SiCl4f TiCl4v &

æ «~~ zbîj ÒÏ~ N~ z"NêöB Öz>wj B '' SiO2f TiO2 «¶¢ W~&.

N~ z" 7öB SiCl4~ Özö ~š W>º Қ(SiO2) «¶

º W" ÿö 'b‚ Ö n;> ªê«ã(critical diameter)

j šš~º– j" 7º‚ †j † ö jî¢ çë'b‚ê j"

·~² wÏ> ®[18]. z" ÚöB  7*Wbš ®bÒ¢

'>æò N Öz>w¢ ãÖ *Ú'ž >wf r" ?, 6

‚ š >wf 1N >w(1st-order reaction)j ~º ©b‚ rJ^ ® [17-21].

(1)

A: SiCl4 or TiCl4 (2)

*  (1)öB Arrhenius &êb‚ >w³êç> k8f r" ?š

¾æâ > ®.

(3)

VB pre-exponential factor, Af ‚Wz ö.æ(activation energy), Ea 8f ­­ ’öB þö ~šB G;B 8š ÒÏ>îb– Table 1ö ¾æÚî.

SiCl4+O2→SiO2+2Cl2 TiCl4+O2→TiO2+2Cl2 dCA

---dt =–kCA

k A Ea

RT---

– 

 

exp

=

Fig. 2. Morphology of aggregates generated by (a) reaction-limited model and (b) diffusion-limited cluster aggregation model.

Table 1. Values of pre-exponential factor(A) and activation energy(Ea) in Arrhenius relation given from other studies

Ea (kcal/mole) A (sec-1) Ref.

SiCl4 98

96±5

1.8×1014 1.7×1014

[17]

[16]

TiCl4 21.2±0.8

18.3

8.26×1041. [18]

[19]

(4)

z B39² B5^ 2001j 10ú 2-3. *¿î Nö" 7Ö¦š†

^ bæ «¶¾ ‚‚šç~ «¶f ?f ·f «¶f 2¢Ú Úÿj ۚB B‚ j&'b‚ ¦O>Ú w÷Ú¢ ;W‚. š

w÷Ú~ ηf ÒҒ–¾" ®~– Ú¦ &ê& ¢~æ p . šf ?š ;& ®~– Ú¦ &ê& 7öB fÚî>ƒ ï

'b‚ Ôjæº Î·j &ê ’–bj *¿î ’–b𢠦ž.

š~ &ê j VF~º–º *¿î Nö(fractal dimension)b‚ ‚

*‚. NB~ V«¶‚ šÚê w÷Ú~ ²*>ãf w÷Ú~ î ï 7b‚¦V ' V «¶ræ~ –Ò ri~ “Ïb‚ r" ?š

;~B.

(4)

¶VFÒW(self-similarity)j <º – w÷Úº îï *¿î(mass fractals)‚ J«† > ®. Ò, îï" ²*>ã, Rgfº r" ? f &ê¢ <º[10, 22, 23].

(5)

VB Nf w÷Ú Ú~ V«¶(primary particle)~ >, Rgº w÷

Ú~ ²*>ã(radius of gyration), aº V«¶~ >ã, k0º ç>, Dfº

*¿î Nöš. š f N-RgDf‚ *® ¾æâ > ®b–, *¿î Nö, Df~ 8f w÷Ú~ *¿î Nöj >~'b‚ J«‚.

öڂž >wVf ?f NöB~ w÷Ú~ ;W";" ;çö &

‚ ’öº 7Ö¦»" ?f j7/ G;VFš j>'b‚ šÏ>

Ú¢ò ‚. šö  ’öB ÒÏB 7Ö¦ š†j BÛ'b‚ J«

light scattering) š†š 6Ò ÒÏ>Ú æº–, w÷Ú ʂö ~‚ 7

(6)

VB cº ;ç>š I0, n, σm" S(q)º «Ò7 ;ê, w÷ÚÚ V«¶~ >&ê, V«¶~ Ö¦ š' Ò w÷Ú~ ’–ž¶

(7)

VB λº «Ò7~ 2˚ θº Ö¦'ê¢ ¾æÞ.

qRg8j Vb‚, qRg 1ž ãÖ Rayleigh ', qRgß1ž ãÖ Guinier ', Ò qRg

[22, 23]. š 7öB w÷Ú~ ;ç" &N®º power-law 'ö &š

Bò ÚÚ¶.

Power-law ', ¯ qRg1ž 'öBº

(8)

 (8)öB Cº ¢w÷Ú~ ’–ž¶ö ~š~º ç>š, ¢>' b‚ C=1, Cpº w÷Ú~ ’Vªö ~š~º ç>š.

(9) n0=nNº * ¦b V«¶~ C >¢ ¾æÚ, w÷Ú ;W "

;öB î‚Ú «¶& W>æ pbš š 8f šB.  (9)ö ~

~š I(q) & q~ log-log ¾*~ VÞVº −Df¢ ¾æÞ. æ‚

w÷Ú~ *¿î Nöj G;† > ®[22, 23].

3. þ

 ’öBº w÷Ú~ ;çj >~'b‚ ‚*† > ®º *¿î Nöj G;~V *š 7Ö¦ ʂš ÒÏ>îb–, 'ÿ j»j

3-1. 7Ö¦ G;Ë~f z" öڂž >wV

Fig. 3f 7Ö¦ G;Ë~~ êÛê¢ ¾æÞ ©b‚ 7 rš: * ö .š&¢ J~~, z" öڂž >wV "*öº ²*ö6j J

~~. ²*ö6 *ö 7ÃV&(PMT; photo multiplier tube)j J~~

 ²*ö6j 'êö V¢ šÿʚB .š&ö ~‚ Ö¦^¢ G

;~&. z" öڂž >wV 6‚ z»b‚ šÿÊV *š šÇË

~¢ šÏ~ F;'b‚ šÿʚB >wV~ *~ö Vž «¶~

;çj G;† > ®êƒ ~&. 632.8 nm 2Ë~ >çOËb‚ Þ7 B He-Ne .š&¢ ÒÏ~&. N¢(chopper)¢ æÂ .š&^º z

" öڂž >wV‚ Úæ, >wVöB WB öڂžf š .š&7j Ö¦Î. Ö¦B .š&7f 7ÃV&j ۚ ÃV . 7Ö¦ G;»ö ®ÚB Ö¦^º "æ 7ö ~‚ žš®(noise) ö jš j" £~V r^ö ‚&‚ S/Nj(signal/noise ratio)¢ ¸¢

ò ‚. ¾B Òå(slit)j ۚB "æ7~ F«j &˂ ÛB~&

. Ö¦B ^ 7öB >çOËb‚ Þ7B ^òj jº‚ ~V r

 ‚® 7jV(laser line filter)‚ 632.8 nm 2Ë~ 7ò jVç~

7ÃV&j ۚ ^¢ î. 7ÃV&j ۚ ƒž–*(lock-in amplifier)‚ ÚJº ^¢ N¢~ "2>¢ ^‚ ~ žš®¢ B

–~&. Ö¦'êö Vž 7^¢ G;~V *š ¶Ú B·B šÇ Ë~¢ šÏ~ 7ÃV&~ *~¢ ;&~² BÚ®. 6‚, z" ö Rg2 1

N---- miri2

i

=

N k0 Rg ---a

  Df

=

I q( )=cI0nN2σmS q( )

q=4πλ1sin(θ⁄2)

S q( )=CCp(qRg)Df

I q( )=cI0n0σmCpk0( )aq Df

Fig. 3. Schematic of light scattering measurement system.

1. Laser 18. Polarizer

2. Chopper 19. Laser line filter

3. Rotator 10. Photomultiplier tube

4. Burner 11. High voltage supplier

5. Axial control motor 12. Beam trap 6. Angular control motor 13. Lock-in amplifier

7. Slits 14. Data acquisition system

(5)

ڂž >wV ƒöB¦V »O˖Òö Vž Ö¦ ^ G;j * (step motor)¢ ÒÏ~ B·>îb–, ʃÎVº V¢ ۚB B ڎb‚Ž ;&‚ *~ BÚ& &Ë~êƒ ~&. Ö¦'êö Vž

^º 5o*Ïb‚ 20oöB 160oræ G;>îb–, š 7öB F;W j šº 'êò F~ ÒÏ~&. z» OËb‚º 5 mm, 10 mm, 20 mm, 30 mm, 40 mm, Ò, 50 mm¢ G;~&. ƒž–*öB ¾ ÒB ^f –šV >÷Ë~(data acquisition system)¢ ۚB 

V~ &ËË~ö Vƒ>êƒ ~&.

Fig. 4º þö ÒÏB z" öڂž >wV‚B Chang" Biswas[1]

& Òς ïš z" öڂž >wV(flat flame aerosol reactor)š.

š >wVº çã 26 mm~ rª &ö Úã 1.6 mm, žã 2 mm~

Êrž.Ê Î^&j jÚ ©b‚Ž .bB &Ê& ²B ê »OË (diffusion flame)~ ãÖ "æ FÚ& ®n;† ãÖ z"~ Fÿš æ

V r^ö, z"öB W>º öڂž~ ;çj G;~, šC~º–

®Ú ôf JNFB ºžš F > ®. >šö ïšz"~ ãÖº ç

® n;'šæ‚ »OËb‚ ;çç~ ¢Nö FÿËj ;W‚.

Fig. 5f 6f  z" öڂž >wV~ z» OËb‚ G;B Nê ª 5 ª.~ >ãOËb‚ G;B Nê ª¢ ¾æÞ ©b‚ z"

öB~ ‚ Nêº ª.‚šb‚¦V 2 mmž æ6öB ‚ Nêž

1,701 Kj ¾æÚî. Nê G;f R Type(Pt 100%-Pt/Rh 13%)~ 

*&¢ ÒÏ~&b–, G;B Nêº "* &Ê~ &~‚ ž‚ *&

;~j(junction bead)‚~ *š ;~j~ Òö ~‚ ¶

3-2. zbî /Ë~ 5 «¶~ 'ÿ j

Fig. 7f z >wb / Ë~~ BÛê¢ ¾æÞ ©b‚B, >w &

Êf Fï–.V(MFC; mass flow controller)¢ ۚ ¢;‚ Fïb

‚ ª.ö />–, >wbîž SiCl4f TiCl4¢ ª.‚ /~V *‚

Ú>&ʂº î²&Ê& ÒÏ>, î²&Ê¢ SiCl46º TiCl4

Fig. 4. Schematic of a premixed flat flame burner.

Fig. 5. Corrected centerline temperature variation along to axial distance, z, at r=0 mm.

Fig. 6. Corrected radial temperature variation at different axial loca- tions.

Fig. 7. Schematic of reactants feeding system.

(6)

z B39² B5^ 2001j 10ú

χb‚ Û"B ÃVçb‚ ª.‚ /®. />º >wbî~

·j ¢;~² ~V *š ª:(bubbler)¢ N ç¶ nö vîb–,

N ç¶~ Úãf ÿ&j ÒÏ~ –&~² 6, Nê –.f “ N>–~ bj N ç¶ nb‚ /Žb‚Ž ¢;~² Fæ~&.

‡j ·j G;~ /B *j G;Žb‚Ž >wb~ "«ïj Ö

;~&.

Fig. 8f «¶~ 'ÿ j¢ ¾æÚº BÛêš. z" >wVö

B W>º «¶f &Ê~ Nêº Ö NšV r^ö N&Ú bÚ

& š ö ã«>š «¶º Nê& ¸f öB Ôf ãb‚ šÿ~º

'ÿ *ç r^ö B*'b‚ N&Ú bÚö ¦O~² B. š‚

«¶~ 'ÿ *çj šÏšB  ’öB W>º SiO2f TiO2«

¶¢ *¶*ãj ۚ &V~V *š j~&. «¶¢ ¦OÒ r ÒÏB 6f 7*ãÏb‚ 6>º ª&¢Ê(cover glass)¢

~ ¢;‚ ³ê‚ ²*B ª&¢Ê& z" öڂž >wV v ª~ Ú¦¢ Û"~êƒ ~&.

4. Ö" 5 V

Fig. 9f 10f '' ª.~ »OË *~ö Vž SiO2f TiO2«¶¢

'ÿ j»j šÏš ª&¢Ê *ö j~ SEM(Scanning Electron Microscope)b‚ R'‚ Òêj ¾æÞ ©š. ÒêöB º :f ?š SiO2f TiO2«¶º .Vö Ö ¢‚ ’V~ ªÖ(monodis-

perse) 2«¶º »OË –Ò& 3 mm

ž æ6öB¦V /ς w÷·Ïb‚ žš V «¶‚ šÚê *

¿î w÷ڂ ;W>îb¾, TiO2 «¶º »OË –Ò& 50 mmž æ 6ræ æ¾ê –~ *¿î w÷Ú¢ ;W~æ p æ V «¶~

’Vò Ã&~º ©j r > ®. Fig. 9º 'ÿ j»j šÏ~

 ’öB ÒÏB z" öڂž >wVöB WB SiO2«¶~ SEM Òêb‚B z» OËb‚ Ã&†>ƒ «¶~ ;ç~ *¿î ’–¢ ¾ æêj r > ®. ß® ‚ z" Nê¢ ¾æÚº *~ž 2 mm¢ æ

¾ 3 mm šçöBº {‚ æz¢ &V† > ®. >š Fig. 10f TiO2«¶~ SEM Òêb‚B *¿î ’–¢ {® ¾æÚ~ SiO2« Fig. 8. Schematic of thermophoretic sampling.

Fig. 9. Scanning electron micrographs of SiO2 particles generated in the flame aerosol reactor.

Fig. 10. Scanning electron micrographs of TiO2 particles generated in the flame aerosol reactor.

(7)

¶fº Ò «¶~ ;çf z» OËb‚ ê¯Nö V¢ –~ ’;~

;çöB æz& ìrj {ž† > ®. šº „öB J«‚ Ξ~ ã Öf ?š SiO2«¶º {ÖB‚' Ξö "Ò~² WËj ~ TiO2

«¶º >wB‚' Ξö "҂ WËj ~V r^b‚ J«F > ® . SEMj ÒÏ~ 2kB w÷Ú~ ;º Fig. 9 5 10~ Ö"öB

¾" {ÖB‚' _f >wB‚'ž &6öB º «¶~ ;W";j BÛ'b‚ ¾ " ®æò «¶~ *B";ö ­ &æ ¦Æ>Ú

¢ F ғj n ®. ©f w÷Ú¢ šº V «¶~ ’V&

Vš~ ¶ò[3, 5, 12, 13]ö jš ç&'b‚ ’² ¾æÂº ©" Fig.

9~ .Vê ¯ z<5 mm~ §f –ÒÃ& 'öB ê ©¾" &

Û'ž «¶~ ’V~ Ã&& ¢&Wj &ææ áŽš ©š. šº

N'öB ¾æ¾º «¶ö &‚ ²Ö(sintering)~ '˚ w÷ڒ

– ;Wö †j ~V r^b‚ '>– G;ò÷~ ¾æÂ V F' JN‚ " >& ®. ~æò š‚ .V '~ JN& vª * Úö &‚ w÷ڒ–~ æz~ jv ï&öº – 'Ëj ~æ pº . N z" ª*VöB~ «¶ ’;zö &‚ J«b‚ ²Ö*çš

"º V·b‚ J«>Ú z. ²Ö*çf [6(melting point) šç~

Nö žÂB ǂ *¿î ’–¢ < ®~ w÷Ú& ²Ö>Ú ’

;~ «¶‚ æz>º ©ö 'Ëj &. ~æò, [6š~~ NêöB º ²Ö*çš /Ï® £zB.  ’ö ÒÏB SiO2 «¶ 5 TiO2

«¶~ [6f '' 2,000 K, 2,100 K šçž ©b‚ rJ^ ®æò, 

’öB ÒÏB z"~ ‚ Nêº 1,701 Kb‚B SiO2«¶ 5 TiO2

«¶~ [6º Ôf Nêšæ‚ ²Öö &‚ '˚ ç&'b‚ Ô

2 «¶º ²Ö

Fig. 11. Trans electron micrographs of TiO2 particles sampled at z=100 mm in the flame aerosol reactor.

(8)

z B39² B5^ 2001j 10ú

*çš "º V·b‚ ·ÏB ©š¢Vº „öB J«B ©¾" æ

³'ž >wb‚ Wb~ ÃV& «¶~ ‚šö Ïò~ «¶~ ‚

šWËb‚ ž‚ ’;«¶~ W ¯ >wB‚' «¶W";ö ~‚

Ö"ªj ¾æÚ&. š‚ >wB‚' Ξ~ 'Ï .º ֓ «¶

~ W˚ >wbî~ >w³ê–.ö ~š «¶~ WË*š –.F

> ®º ©j ¾æÚæ‚ ^‚ ’V'~ «¶ö &‚ ’V–.

&ËWj B~ ®. š‚ ¢6f Fig. 11~ ¶ò 5 Table 3~ ¶ òö ~š º& J«B. Fig. 11f ²>w~ ïj Œ¢ æzÊ

šB >wV~ vªOË *~ z=100 mm~ ;B *~öB TiO2

Ú¢ ÷~ ¾æ¾º w÷Ú~ ;çj TEMb‚ &V‚ ©š. Fig.

11öB ¾æ¾º "º ;º ²>w~ ïj~ Œ~ Ã&ö V¢

«¶~ ;çö 'ËÖ;ö 'Ëj "º {ÖB‚; ;" >wB‚;

;š "ºV·b‚  ";öB w÷Ú¢ šº V«¶~ ’V&

ïj& Ã&~š z"Nêº ¸jæº >š "Úê *’bî~ ³ê ö &‚ Ö²³ê& ç&'b‚ ·jê. š r^ö «¶~ W";

f Ö²³ê& Ôjöb‚ žš ¾æ¾º Öz>wN~ 6²f NêÃ

&ö V¢ ¾æ¾º Öz>wN~ Ã&ö Vž ãç' 'Ëj A²B . æ‚ *’bV V«¶& ;W>º .V>wöB¦V j*‚ w÷Ú& ;W>º ‚«êræ *'b‚ ;ê~ Nšº ®

š ";öB Nê~ †f w÷Ú ’–Ö;ö ¢Ú¾º ²Öö ôf

†j ~º ©f ª«~. ~æò ïj& Œ= 0.98öB Œ= 0.75‚

æÿ>º ÿn z"Nê N& 150oC šÚ¢ Fæ~V r^ö ïj

V¢B Fig. 11öB Œ= 0.98~ ãÖ& Œ= 0.75ž ãÖ  – V«

¶¢ &æº šFº Ö²¦—b‚ ž‚ *’bî~ ÖzN 6²ö V

ž~º >wB‚' w÷·Ï~ jòšöš ç&'b‚ z 7º‚ V·

b‚ ·ÏB r^b‚ 6B. Table 3f Fig. 11ö ¾æÞ ' –šö B~ TEM ÒêöB ¾æÂ ’;~ ;~ V«¶¢ 'ç¾Ò~

;ï'ž ï’V¢ ¾æÞ ©š. çÏ~ 'ç¾Ò ²*ÞÚ[24]

¢ ÒÏ~ V«¶¢ F† rº «¶~ ;çš ’;j &æšB

«¶~ 'Ú¦~ «zê(gray level)~ ÞN& ¢;8 š~¢ &æº

©òb‚ F>î. š-² ‚ šFº v B šç~ V«¶& oö B w÷Ú¢ š ãÖ «¶~ TEM «zê& ¢æV r^š.

Fig. 12º  ’ö ÒÏB z" öڂž >wVöB G;B Nêö

~–~ >wbî~ ³êæz 5 >w³ê¢ ª.~ z» OËb‚ ê ւ Ö"š. z>w GšöBê >wbž SiCl4º >wV «’ö B f * Úö B*'b‚ ªš>  êöº –~ ªš>æ pº . šº Wbž SiO2«¶~ GšöB " r, z"~ ‚Nê¢ ¾ æÚº 2 mm æ6j æÎö V¢ «¶š B*'b‚ W>  š ê Nê& 6²Žö V¢ z šç~ «¶~ Wf B~æ p, w

»ö ~‚ «¶WËê šÚææ prj ~‚. š‚B  z" >

wVöB~ SiO2 «¶~ "º WË V·f «¶~ {Öw÷ö ~‚ W ˚ "º WË V·ªj {ž† > ®. >š TiCl4~ Öz>wö ~

š W>º TiO2«¶~ ãÖö, TiCl4~ >w³ê ç>º ª.~ * º >w *>¦ž N'öB öò jî¢, &N'öBê TiCl4 ª

š& 곚B ê¯Nj ~‚. ¯ æ³'b‚ ê¯>º TiCl4 ªš

º æ³'ž TiO2ÃV~ Wj ~~,  WB TiO2ÃVº Všö TiO2«¶& šÒ~º ãÖöº î‚Ú TiO2V «¶~ W,

¯ î‚Ú ›;W º Všö WB TiO2«¶~ ‚šö w»>Ú ê. š w»*çf Všö W>Ú ®~ TiO2 V«¶~ ’V¢

66 Ã&ʺ ·Ïj ~æ‚ ‚«'b‚ W>º «¶~ ;çf „ B J«‚ >wB‚' Ξö ~~š ’;~ «¶‚ WË~² Nj r

> ®. š‚B TiO2 «¶ W~ "º V·f «¶~ ‚šö ê³'b

‚ W>º Wb~ ÃV& «¶~ ‚šö ¦OŽb‚Ž ’;ö &r Table 2. Experimental conditions used for particle aggregation in the

flame aerosol reactor

Air flow rate, cm3/min 3411

Propane flow rate, cm3/min 129

Equivalence ratio 0.90

Carrier gas flow rate, cm3/min 60

SiCl4 feeding rate, g/min 0.0758

TiCl4 feeding rate, g/min 0.0419

Table 3. Size of basic unit particles in the aggregates with respect to the combustion equivalence ratios

Equivalence ratio, φ

0.75 0.80 0.85 0.90 0.95 0.98

Number of samples 23 13 18 17 15 10

Mean diameters(nm) 22.1 26.8 29.9 25.8 34.3 34.5 Standard deviation in diameters 15.8 14.5 16.2 15.8 19.3 16.2 Minimum of diameters(nm) 11.8 21.2 22.2 18.6 19.8 19.8 Maximum of diameters(nm) 32.8 38 44.9 40.3 49 49

Fig. 12. Normalized chemical concentrations and reaction rate constants in the flame aerosol reactor along to axial distance.

Fig. 13. Angular scattering intensities by SiO2 aggregates and its frac- tal dimensions along to axial distance.

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Ú «¶‚ W˚ &º w»š æV'ž WË V·ªj {ž† > ®.

Fig. 13öB 14º '' SiO2, TiO2«¶~ Ö¦ÇV ’Vö Vž Ö¦

;ê¢ log-log ¾*‚ êz ‚ ©b‚  (9)ö Všš ¾*~ V ÞVº *¿î Nöj ~~ ¾*~ ç&'ž Ö¦;ê ’Vº «

¶~ ’V¢ ~‚. SiO2«¶~ Ö¦ ¾*öB ª.~ z»OË

*~ö V¢ Ö¦;ê& Ã&~º ©f *š æÎö Vž w÷Ú~

’V& Ã&~ ®rj ~~, *¿î Nöš Ã&~º ©f w÷

³ ê¯Nö V¢ w÷Ú~ ’–º ǂ ÒҒ–~ *¿î ’–&

>Ú 6j r > ®. ‚«'b‚ *¿î Nöf 1.83~ 8j ¾æÚ

 ®. šº  z" >wVöB WB SiO2 «¶~ w÷ڒ–º

*;'ž {ÖæV' w÷Úªj ¾æÞ. >š TiO2«¶~ Ö¦ 

¾*öBº ª.~ z» OË *~ö Vž *¿î Nö~ æzº –~

ìš 2.81öB 2.94~ 8j ¾æÚî. Ò, z» OËb‚ Ã&†>

ƒ Ö¦;ê~ ’V& Ã&~ ®. šº w÷Ú~ ’V& *~ Ã

&f Žþ Ã&~ ®rj ~~ «¶~ ;çf WË .V¦V W

Ö"º *¶*ãb‚ &V‚ Ö"f j" ¾ ¢~~ ®rj {ž

† > ®.

Fig. 15º  ’öB WB TiO2 «¶~ XRD ªCÖ"¢ ¾æÞ . XRD ªCÖ"  ’~ z" –šöB WB TiO2«¶º 7

æ‚  ’öB ÒÏB z" öڂž >wVº Bê TiO2 /

WB «¶~ ’V 5 ;çš šæ‚ ·f ’V~ TiO2«¶¢ z

+~¶ ~º bÚö z+~² >š /& <º j‚š'š Ã&~

ëÏ ªÚ Wj *‚ BÚæ>‚B ‚ÏNö V¢  ¦&&~

~ ªÚ¢ W† > ®j ©b‚ Îê. ‚ žš, æîj(titania)

®j ©š.

5. Ö †

.b ïš z" öڂž >wVÚöB >wbî~ >w³êö V

(1)  ’öB ÒÏB z"Nê –šöB SiO2 «¶~ ‚«;çf

ǂ ÒҒ–¢ <º *¿î ’–~ «¶& WNj {ž®b–,

«¶~ ‚« ;çj æV~º "º w÷Ú ;W V·f {Öw÷ªj r~, šº «¶ ;ç Ξ 7 {Ö B‚' Ξö šNj r > ® î.

(2) TiO2 «¶~ ‚«;çf ’; «¶& WNj {ž®b–,  

’~ z" –šöB TiO2«¶~ ‚« ;çj æV~º "º w÷Ú ; W V·f Wb ÃV& «¶‚šö Ïò~ «¶~ ‚šj WË

ʺ w»š æV'ž w÷Ú ;W V·ªj r > ®î, šº >w B‚' Κ TiO2 «¶ ;W~ "º V·ö šŽj {ž®.

(3) ²Ö*çš ç&'b‚ £z>º [6 š~~ z" NêöB  W>º ’;«¶~ WËj >wbî~ >w³êö Vž «¶~ ‚šW Ë &6b‚ J«>î.

(4) >w æV' w÷Ú ;W Ξj Všº TiO2«¶º >wbî~

>w³ê¢ –.Žb‚Ž «¶~ WË ³ê¢ –.~ š‚ «¶ ’ V¢ –;† > ®º &ËWj B®.

(5)  ’ö ÒÏB z" öڂž >wVöB WB TiO2 «¶º

>wNê 5 «¶~ WË*j –.Žb‚Ž «¶~ ’V 5 j‚š

'š BÚB çë' ¦&&~~ ªÚ Wö wÏF > ®j ©š.

6 Ò

 ’º ‚“"Ò ß;V.’Òë("B®^: 98-0200-03-01- 3)~ ¢¦‚ >¯>îb– æöö 6Ò ãî.

ÒÏV^

A : pre-exponential factor a : radius of primary particle

C : constant dependent on the form of the single cluster structure factor Cp : constant dependent on the size distribution of the aggregates Cx : chemical concentration of x-component

c : calibration constant Df : fractal dimension Ea : activation energy I : light intensity k : reaction rate constant k0 : constant of order unity mi : mass of i-th primary particle N : number of primary particles Fig. 14. Angular scattering intensities by TiO2 aggregates and its frac-

tal dimensions along to axial distance.

Fig. 15. X-ray diffraction analysis of TiO2 aggregates generated in the flame aerosol reactor.

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z B39² B5^ 2001j 10ú n : aggregate number density

n0 : total number of monomers per unit volume q : magnitude of scattering wave vector R : gas constant

Rg : radius of gyration

ri : distance from mass center to i-th primary particle S : structure factor of the aggregate

T : temperature

t : time

ÒšÊ ^¶

θ : scattering angle

λ : wavelength of the incident light σm : monomer scattering cross section

^^ò

1. Chang, H. S. and Biswas, P.: J. Colloid Interface Sci., 153, 157 (1992).

2. Chang, H. S., Chang, H. K., Hong, H. Y. and Won, Y. S.: Environ.

Eng. Res., 3, 79(1998).

3. Yang, G. and Biswas, P.: Aerosol Sci. Technol., 27, 507(1997).

4. Ehrman, S. H., Friedlander, S. K. and Zachariah, M. R.: J. Aerosol Sci., 29, 687(1998).

5. Ulrich, G. D. and Riehl, J. W.: J. Colloid Interface Sci., 87, 257(1982).

6. Chung, S. and Katz, J. L.: Combust. Flame, 61, 271(1985).

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Opt., 28, 530(1989).

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10. Megaridis, C. M., Dobbins, R. A.: Combust. Sci. and Tech., 71, 95(1990).

11. Cho, J.: Ph. D. Dissertation, Seoul National Univ., Seoul, Korea(1999).

12. Akhtar, M. K., Lipscomb, G. G. and Pratsinis, S. E.: J. Aerosol Sci., 21, 83(1994).

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Soc., 59, 146(1990).

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