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Decomposition of PET in High Pressure Subcritical Water

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(1)HWAHAK KONGHAK Vol. 40, No. 6, December, 2002, pp. 709-714.    PET

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(4)     (2002 8 22 , 2002 10 18 ) *. Decomposition of PET in High Pressure Subcritical Water Seung-Hee Chung, Jung-Hoon Lee, Jae-Jin Shim*, Jae-Seong Kim and Sunwook Kim† School of Chemical Engineering and Bio Engineering, University of Ulsan, Ulsan 680-749, Korea *School of Chemical Engineering and Technology, Yeungnam University, Gyeongsan 712-749, Korea (Received 22 Augsut 2002; accepted 18 October 2002).      poly(ethylene terephthalate)(PET)

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(8)  ^_1 `a IV b LK 54.4 kJ/mol (Q . o. Abstracts − To investigate the decomposition kinetics of poly(ethylene terephthalate) the high pressure molten-polymer injector has been devised. Using the experimental apparatus equipped with batch reactor and high pressure molten-polymer injector the decomposition of PET has been performed at constant pressure of 250 bar and 300, 320, 340 oC, respectively. At each temperature conditions the conversions after initial 1 minute have shown very high values such as 76-90%. As the temperature increases the conversion reaches more than 98% at 10 minutes. Based on the second order reaction model the reaction rate constants have been obtained. We can calculate the conversions within 2% errors utilizing optimized rate constants. The activation energy for the decomposition of PET at subcritical conditions has shown to be 54.4 kJ/mol. Key words: PET, Decomposition, Subcritical Water, Rate Constant. 1..  . r ,   ^_s ( ab ?t u v L8S wxy# z  {"12. W>  n | 8. ab G (ab }~K € NI P 1w‚ , iƒ  }~ Tohoku MK €„ BC M †()ab‡(NIMCR) > Uˆ WHI V

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(152)    PET . 713. º`# œ 89 ‰ð# Œ8S TPA [A  ê (1) # ( 89 2’ êK ü1  _ W 2. d C COOH --------------------- = kC EL CH 2O – k'C COOH C OH dt. (3). 9(I C  bÍc{ ; S, C K C  =þÍ ÒJK B S> ýý  H, C  [As EG S> &2. ä&   vW k " Ç <W

(153) ‰  ÂvW1 k'- a. Ç hJ ÂvW>  @2.  RF¶1 ζ £ õ . B G [AB S> RF¶ %W 2’K ü1  _ W 2. COOH. EL. H2O. OH. C COOH = CELi ζ, CEL = C ELi ( 1 – ζ ). (4). C H O = CH Oi – CELi ζ, COH = C COOH. (5). 2. 2. 9(I C Ž C   ( ÿùs PETŽ H O ( S> &2. ê (4), (5)> ê (3) ù89 "8Ü ELi. 2. H2Oi. CH Oi  dζ ------ = kC ELi ( 1 – ζ )  ----------- – ζ – k′CELi ζ 2  C ELi  dt. (6). 2. 1 ê# p

(154) 8Ü Œ h RF¶ kL> 2’K ü- ê  _ W 2. 2ζ + S – Q2ζ + S – Q ln ----------------------– ln -----------------------2ζ + S + Q t 2ζ + S + Q. 9(I SŽ Q 2 kr + k4kr S = – -----------, Q = S – -----------k – k′ k – k′. = C ELi Q ( k – k′)t. Fig. 6. Calculated conversion of PET at 320 oC using optimized reaction rate constant.. (7). t=0. 1⁄ 2. C 1, r = ----------->  @2. C H2 Oi ELi. Table 2. Optimized reaction rate constants based on second-order model Temp.(oC). k(g PET/mol/min). k'(g PET/mol/min). AARD(%)*. 300 320 340. 7.724 11.090 16.280. 0.907 4.082 13.27. 1.36 1.57 3.54. ∑ ζexp – ζc al ⁄ ζexp * ---------------------------------------n. Fig. 7. Calculated conversion of PET at 340 oC using optimized reaction rate constant.. ¢ 2Ó  º`# p 8 {³ ?t> pL89  Âv W> b8S 1 ,r1 Table 2 "w 2. ä& Table 2 pLs  ÂvW> 1 89 RF¶# ;& v>Ó< .  S ij 2% " >Ó {³ ?t>  _ W ’# µ W 2. 300, 320, 340 CI {³ ÒKŽ ;j> Fig. 5-7 . kS 300 CŽ 320 C  (SI R S ô l W& ;ÒK> «1  340 C  Œ1 ‚5  h ;s ,1 {³j«2 Þ- ,# «1 2. d< ¹O ‚l Ü " K a  ‰ 2Ó  º` ;s ,1 {³ j«2 Þl ; G# «1 ( õ  ~ ab«2 ¹- d I

(155) ‰ # WŠ8 1> ‰ð8( ö‰I 2 º`# p ‰ ‘ › [ýs2. ~ ab> è‰ Ù-   vW> 1 89 Fig. 8K ü- Arrhenius o. o. o. o. Fig. 5. Calculated conversion of PET at 300 oC using optimized reaction rate constant.. HWAHAK KONGHAK Vol. 40, No. 6, December, 2002.

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(158) ‰   & |AL¼‚ 54.4 kJ/mol ;™S 1 ,Campanelli N [13] ,Ç 55.7 kJ/molK œ& ,# «1 2..   ~ ab &€KMZÕ 4p(ab(KDno: R01-2000-000abÁŽ 2001M¯ F5MÝ M)ab EAÁ ‚Y ‰ WŠ™pÆ2. 00324-0). . Fig. 8. Arrhenius plot for the hydrolytic decomposition of PET.. # 8 Ù- PET <W

(159) ‰   & |AL¼‚ 54.4 kJ/  ;™S 1 ,- Campanelli N ,Ç 55.7 kJ/molK œ & ,# «1 2. æ‚m ~ abI ó89 D& e ø

(160) ? Pù±j> | 8 {³±j G ¥¦# E3 «´8Ü ~ ab«2 ¹- d W vñ {³ <@82 [ý PET Åq1 OÆ 2Q& 

(161) ?

(162) ‰ | ‘ W # › ( s2. plot mol. 4..

(163) . ~ abI poly(ethylene terephthalate)(PET) <W

(164) ‰  # }"& e/K O d(300 C, 320 C, 340 C) 8I {Œ89 {³Eg h [ABÇ terephthalic acid(TPA)Ž ethylene gylcol(EG)

(165) $> b8 2Ó  º` (& 1JpÇ ‰ð# { Œ82. 

(166) ?> Pù& TŒ îïŒ! ( RF¶1 0.683-0.810 OP ×2V ,# «S 1›- 

(167) ? PùK"K  Ô îïK "I

(168) ‰ s Q ‰ ›12. ~ abŽ ü1 e ø

(169) ? Pù±j> œ 8’ ÷b8 v PET< (

(170) ‰w òì ô «O q" e ø

(171) ? Pù±j> œ 8‚ ÄHÜ . ( dU ¬ 

(172) PET<

(173) ‰w {³1 ÷<@ 8  [ýs2. ¢ W EgK ü- o 7 ¹- dI {³ # WŠ8( ö‰I ‚3 {³¥¦I 

(174) ? PùŒ# ‡L 8 N i& x< w ‘ ›12. ~ ab d/öHI PET  ( 1

(175) H RF¶1 76-90%< ‘ " n ¹H d< <% h RF¶ X ,# «1  Œ1 10

(176)  ·8l  Ü RF¶ ,- 96-99% 1v ¹- RF¶#  H™ COOH S 1JpÇ WjÇ 10.4 mmol/g PET , Ï8l s2. {³ ?t> ‰ð8( ö89 2Ó  º`# p 8  Âv W> b8S 1 ,# 1 89 v>Ó< ij 2% " Þ>Ó HI RF¶# ;£ W ™2. 300 CŽ 320 C  (SI RS ôl W& ;ÒK> «1  340 C  Œ1 ‚5 h ;s ,1 {³j«2 Þ- ,# « 1 2. d< ¹O‚l Ü " K a  ‰ 2Ó  º ` ;s ,1 {³j«2 Þl ; G# «1 ( õ   ~ ab«2 ¹- dI

(177) ‰ # WŠ8 1> ‰ð8( 250 bar. o. o. o. o. o. o.  40 6 2002 12. CCOOH CEL CELi CH2O CH2Oi COH. : concentration of carboxylic acid [mmol/gPET] : concentration of ester linkage [mmol/gPET] : initial concentration of ester linkage [mmol/gPET] : concentration of water [mmol/gPET] : initial concentration of water [mmol/gPET] : concentration of ethylene glycol [mmol/gPET]. k k' r t. : forward reaction rate constant [g PET/mol/min] : backward reaction rate constant [g PET/mol/min] : ratio of initial concentrations of water and ester linkage : time [min]. 

(178) ζ. : conversion.  1. Shanableh, A. and Gloyna, E. F.: Water Sci. Technol., 23, 389(1991). 2. Li, R., Savage, P. E. and Szumukler, D.: AIChE J., 39, 1(1993). 3. Holgate, H. R., Meyer, J. C. and Tester, J. W.: AIChE J., 41, 637(1995). 4. Lawson, J. R. and Klein, M. T.: Ind. Eng. Chem. Fundam., 24, 204 (1985). 5. Watanabe, M., Hirakoso, H., Sawamoto, S., Adschiri, T. and Arai, K.: Proceeding of 4th ISSF, B, 591(1997). 6. Klein, M. T., Izzo, B., Harrell, C. L. and Adschiri, T.: Proceeding of 4th ISSF, B, 543(1997). 7. Sasaki, M., Kabyemela, B. M., Adschiri, T., Malaluan, R., Hirose, S., Takeda, N. and Arai, K.: Proceeding of 4th ISSF, B, 583(1997). 8. Kabyemala, B. M., Takigawa, M., Adschiri, T., Malaluan, R. M. and Arai, K.: Proceeding of 4th ISSF, B, 547(1997). 9. Kabyemala, B. M., Takigawa, M., Adschiri, T., Malaluan, R. M. and Arai, K.: Ind. Eng. Chem. Res., 36, 2025(1997). 10. Kabyemala, B. M., Takigawa, M., Adschiri, T., Malaluan, R. M. and Arai, K.: Ind. Eng. Chem. Res., 36, 1552(1997). 11. Adschiri, T., Sato, O., Machida, K., Saito, N. and Arai, K.: Kagakuikougaku, 23, 505(1997). 12. Kim, B.-K., Hwang, G.-C., Bae, S.-Y., Yi, S.-C. and Kumazawa, H.: J. Appl. Polym. Sci., 81, 2101(2001). 13. Campanelli, J. R., Kamal, M. R. and Cooper, D. G.: J. Appl. Polym. Sci., 48, 443(1993). 14. Kao, C.-Y., Wan, B.-Z. and Cheng, W.-H.: Ind. Eng. Chem. Res., 37, 1228(1998). 15. Yoshioka, T., Okayama, N. and Okuwaki, A.: Ind. Eng. Chem. Res., 37, 336(1998)..

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