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wrstiaLes t_arnun oakiand 1 511a 639 7762 P.@3 <br /> I tMP Sf3 QPP <br /> RE$1 ES RI131 1x151 Er ^' ars .. t:: �± F• :T�s ;�:xxr j <br /> kP4�5+tf r C! g `t �+v S - Q� �d ' <br /> t I. Go6onaIM9hel1 carbon <br /> � + JTri chlorOle <br /> tfsylenIt , <br /> Coat-ba.%O l Carbon, E3ertien I ! <br /> S I?' I <br /> Acetone € <br /> r#1 <br /> I <br /> ,: .: .fz i4 104 11,400 t0�04 a .OD,fJ00 ;.:;-' a;: r� <br /> .t }} :31D w y}l0. !'SU 6!) � "74;•..•�D' � i <br /> �: Porgy r !s)s,e;gstroms "`I Reiailtre <br /> i <br /> hiriltait <br /> Y f .RH +? `.:,. <br /> VIM.s�t�rclewlcz <br /> ' FIGURE 1(1; l.fDilfierent sfltrrces nrr,.t¢antivatkct carbon with vaslly different pore structures-Micrepgr�sity is:wefl daVlNoped in <br /> VWXCOwt-shell ;4'C#nost',portes int the t-MA range),While coal-baSed carnons h#!ve severai zones n!mesa-and macropaNsity;By M <br /> PICttfAg the d rh4ti4es of pare voiunme'f!and radius,these relative differences In parostty charactivi etks are then#uatad- <br /> FlG1JSE 2(C Ill Since:the retatitre qumidity of 1he YQC s"arn hinders carbon's adsorpflarl cap�lcEly,saps must b7 taken 1O <br /> rninirhfze the m unt of mgistUre in thr inftent stream <br /> I � <br /> I <br /> i titinefi faQax;`1elforrMatidn of earlaoiis aigttificant water retention a$RE tops tore, and show�Eects of W6'oh the <br /> t with;welt ae eked.rnicrtrgorosity aid 50%.At this point, tapiIlary condensa- adsorption of behxene! , <br /> rttrrrun►Stafa4.•e axx a , tion becomes important, and it in- <br /> VOC adsull Ptil by activated carbon creases with increasing RH until the .MuIti talenteii Este <br /> is a physical prReess,invoNing vain der microporous structure of the cai7bon is Carbon•adsorpWri technologies .for I ; <br /> j Waals force Yliis.weak'exotherrt}ie cam ylete}y filled with.water. VQQ removal .foqus .6n two!:applies- <br /> i -ir; e4cm l' r�tc's between 2 ands 5 T6 reduce the effect of RH an $ tions:The recov,�ery of valuable indus- <br /> 'kcalhnole of eitr carbon's adsorption capacity, the M04- 'trial solvents for risuse,and the remov- <br /> 1 A.;phenozo noii called tapilIary con- tore:content of the stream can be xe- al of VOCs for air_�Ou ttion cflntral and . <br /> .dens tion ows eerbil .carbons tri dix4d in ore of two ways,Because All purification. j 4 <br /> hold; e YpC I at,a Capacity bf is a strong function of the gas tempera- To ensure a0inpteti'jtpted operation, <br /> 3U�++ar more f#Meir weight[x].As t ie tore,the gas stream can either be heat =bon-hued systems are noritially op- <br /> arbo n-b sedsems <br /> I play a big role <br /> I ' l . j <br /> ! in pollution :prey n#ioh <br /> and solvent reaorery <br /> eeatoantrad ' of the,VOC,in the ZL- ed by 20 lyp,or,it can be cooled funs � <br /> erated in'a cyclic p nein Adsoron is <br /> s eous;snc eaples,multiple laye�s ' to condense out moisture,and then re- switched betwe6 two Meds,so that one ' I <br /> of orie ol ic compound iiuild up bu heated to reduce the relative humidity is regenerated 4ile;the cther is in ' <br /> the walls of W''hotx livres. At still to below 50%. service. Regeneration, is initiated at. <br /> highitr VOCj•oneentrations,this build- Since carbon adsorption is an eso= cording to a timed addorption jcyde, or j <br /> ulp.iAtimatel' causes VO Cs to collect' therink process, adsorption efficiency when breakthroll (xhe fust detect, <br /> a tquid in tli sm.allbst pores_ ! will be reduced as the temperature of able appearance of the organic cam• <br /> The rel" h74m'l i and t ei r ' the stream being treated is increased, pound in the adsorber efflll has I ! I <br /> perature of. ie VOCr'`ladeit Sim=also Por this reason,it is preferable to re- been observed. 1 <br /> direly affe the'Carbo? "s ability 4 duce RH by chilling, so that a cooler To restore the"spent"bed its origi- <br /> ,adsu,I and z of l h organic levels- stream ig delivered to the Carl]o3l Keds. nal fartn,.a gaseau{�regenerating agent I <br /> The;sdsozpt� n ;oapacitg is;diminished In general,the efffect of temperature. is.passed thronglx it at elevated tem- 1 I <br /> signif tan ly asi the";RH of the VOC on a caabon's adsarption capacity is' peratures.Theadsorbe�VQCz>z'aleculea � ! <br /> Weim exc s50 (pYgut a 2). considerably legs than the effect of rel- am desurlied and callerted far�disposal, , <br /> A idok at vlrltex�tsothgm curve for ative humidity.Figtlres.d.axed a provide or for further tmatmeiit and reuse. <br /> a "I--based carbo '( igvre 3) shows a comparison of the RH and tempera- I?eg)endiug an the C{?nstrgi,itS or re i <br /> i I I <br /> :. r <br />