CLEAN TECHNOLOGY, Vol. 15, No. 1, March 2009, pp. 60-66
Adsorptive Removal of TBM and THT Using Ion-exchanged N a y Zeolites
Gap Soon Jung, Seok Hee Lee, Jae Kee Cheon, Jae Wook Choe,+ and Hee Chul Woo*Department of Applied Chemical Engineering and 'Department of Safety Engineering Pukyong National University
San 100 Yongdang-dong, Nam-gu, Busan 608-739, Korea
(Received for review February 25, 2009; Revision received March 23, 2009; Accepted March 24, 2009)
3447)&3';~] L L -$7) 3$%%0,! T H T * T B M q 33 417-1s 4 4 N a y xilgqo]Erlj$ ol$-IiH $4
3z8
$a&S)$q. NaYq] ~$3 xgq +-%714 -2% @$-A]?~J s-I;F%q %bJQ 2 ~ 3 f 7 1 4-IiH Li,K, Fe, Co, Ni, Cu, Ag 52-l
s+;-a]&og-
ol&ij!%$)%Oq, 01sy # A ] l l T Q i T B M q &%$ A13 0114
$8)$+. rt 7$i+ CU-Nay, Ag-Nay, NaYd[Jhj qg +b%@ll nl8H
W r ,
T B M qs)st-.l)-%-e%*l
+?A) it~ + % 9 q , Cu, 4 7 ) ol&j!@@ A)gi+l54 $71@ *Ad4 %Ad qED11 01&5011 gliiH +?P 3%
3 %
qqg 323. A t S q O j a q . *go1 4 - N a Y 2 . q &A\ 53 C u - N a Y qa+,
C u q 9x1 E01% 7)&cll 0.5
M q &
5.21$~4.0-2 ol&izg)Tti! Cu-Nay-0.57). 71% && irt+Sq% li%0 q, T H T q d6H 1.85 nunol-Slg, 'TBMq] d84 0.78 rnrnol-S/& qq qE$-q 24. 2.213T H T q 33
-
~ A J q ~ q ~ l ~ N a y , Cu-Nay-0.5 5 3 2 q ] 4-Ii)q 2 Zp17) M%Oq, T B M q $3 g A d @ d q ~ l q 4 9 Cu-Nay-0.5 $$qA]ot)hj N a y ji!.q &A] % 3 S ) % q .
Abshact : Adsorptive removal of tetrahydrothiophene (THT) and tert-butylmercaptan (TBM) that were widely used sulfur odorants in pipeline natural gas was studied using various ion-exchanged N a y zeolites at ambient temperature and atmospheric pressure. In order to improve the adsorption ability, ion exchange was performed on N a y zeolites with alkali metal cations of ~ i ' , ~ a ' , K+ and transition metal cations of cu2+,
~ i " , CO", A ~ + . Among the adsorbents tested, Cu-Nay and Ag-Nay showed good adsorption capacities for THT and TBM. These good behaviors of removal of sulfur compound for Cu-Nay and Ag-Nay zeolites probably was influenced by their acidity. The adsorption capacity for THT and TBM on the best adsorbent Cu-Nay-0.5, which was ion exchanged with 0.5 M copper nitrate solution, was 1.85 and 0.78 mmol-S/g at breakthrough, respectively. It was the best sulfur capacity so far in removing organic sulfur compounds from fuel gas by adsorption on zeolites. While the desorption activation energy of TBM on the Cu-Nay-0.5 was higher than Nay zeolite, the difference of THT desorption activation energy between two zeolites was comparatively small.
Key words : Adsorbent, Odorant, Adsorptive desulfurization, Zeolite
* To whom correspondence should be addressed.
E-mail: [email protected]