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第 9号 2007年

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ガラス状炭素球の空気賦活

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T Abstract Pore deve10pment in glass-like carbon spheres with oxidation indryair was s旬di巴dthrough the measurements of oxidation yie1d, various pore parameters and pheno1 adsorption. The dev巴10pmentof pores was understood by the master curves at 400 oC for oxidation yie1d,巴achpore parameters and pheno1 adsorptivity.

The resu1ts showed that the conversion between oxidation temp巴rature and time was possib1e for por巴

deve10pment by air oxidation, i.e., at a temp巴raturebetween 355 and 430 oC in a flow ofdryair. Por巴 deve10pm巴ntwas supposed to proce巴dprincipally the opening of closed pores existed originally in glass-like carbon to form ul位amicropores,followed by the collapse and en1arg巴mentof u1仕anncroporeto macropore through supermicropore and mesopore. 1.Introduction Activated carbon has p1ayed important ro1巴s since

pre-historica1巴:raand now b巴come even mor巴 important

mat巴ria1s in various fie1ds of techno1ogy. Indus仕ia1 app1ications of activat巴dcarbons to modem techno1ogy, for 巴xamp1巴s,applications to car canister, the storage of natura1 gas, th巴 巴l巴C仕odemateria1 of e1ectric doub1e 1ay巴rcapacltor, 巴tc.,d巴mands仕ictcontro1 of their pore s仕ucturel-3). Th巴 most irnportant process for the production of th巴seactivated carboIfs is activation, which has b巴enstudied by a number of researchers and engineers企omdiffer巴ntpoints of view and a1so different activation proc巴sseshave been d巴V巴10ped,for examp1e, using either steam, ZnClz or KOH in order to deve10p micropores and to have high surface ar巴ピーの‘ This activation process is th巴 oxidation and gasification of precursor carbons, most of th巴m being hard carbons and containing a 1arge amount of macropores One of the authors has been studied the process of gas activation by se1ecting carbon spheres, which w巴reprepared 企omph巴no1resin and had glass-1ike carbon nanotexture, as the origina1 carbon samp1e7-27) In our previous paperI4), the activation proc巴ssof hard carbon spheres in an a加 osphere of wet air at different temperatures and residence times was understood by a master curve for the yie1d a日teractivation, which suggested the conv巴rsion between oxidation temperature and time. On th巴sam巴carbonspheres, the activation process by dryair was investigated through the measurem巴nts of various pore s仕uc同re paramet巴rs,in addition to activation yie1dl6, 17)and a1so adsorption behavior for various organics in th巴ir aqueous solutions were understood by the master curves for each adsorbates as functions of oxidation tempera札lre and tirne23) A1so adsorption behavior of methan巴gasinto air-oxidized carbon spheres was s知died20). Inthe present paper, pore dev巴10pment in carbon spheres in an atmosphere ofdryair was discussed through master curves for each pore parametersl6, 17). ↑愛知工業大学工学部応用化学科(豊田市) Facul1y ofEngineering, Aichi Insti旬t巴ofT巴chnology 2. Materials and Characierization Techniques 2.1 Materials

Carbon spheres prepared合oma reso1-守pepheno1 resin spheres by carbonization at 1000 oC wer巴 se1ected,which had the particle size of ca. 10μm. Carbon spheres of 10.0 g were p1aced in an a1umina boat (50 x 90 m m and 10 m m d巴叩)and heated at different t巴mperaturesbetween 355 and 430 oC for different p巴riods丘om1 to 100 h in a flow ofdry a1r m a札lbu1arfumac巴(60m m in inner diameter). The air was dried by passing through a silica g巴1co1umn and then passing on the surface of P20S with a flowing rate of 50 mL/min. After air oxidation, oxidation yie1d was caIcu1ated from the mass 10ss during oxidation process 2.2 Pore structure characterization On carbon spheres thus oxidized, adsorptionld巴sorptlOn

isotherm of N2 was measured at 77 K. From the isotherm

measured, diffe

rentpore param巴tersw巴redetermined using

different ana1ytica1 methods‘ BET surface紅 白 was ca1cu1ated using adsorption data up to the re1ative pr巴ssure

P/PO 1ess than 0.3. Through the ana1ysis by so-calledαs

p1ot, tota1 surface ar巴 丸 田tema1surface area and micropore

vo1ume were ca1cu1ated, and microporous surfac巴ar巴awas

derived as a ba1ance between tota1 and extema1 surface areas Based on DFT ana1ysis, pore size distribution in the size range corresponding to micropores (up to 2 nm) was determined. From the cumu1ation, the vo1ume of micropores(く2.0nm) and a1so that ofuItramicroporesく(0.8 nm)w巴reobtain巴d. The vo1ume of mesopores (2~ 50 nm) was deteIDlined by using BJH method. SEM observation on the surface of carbon spheres was performed und巴rthe e1ectron b巴 創nacc巴l巴ratedby 10 kV. Adsorption of pheno1 from its aqueous solution was determined on the carbon spheres oxidized. The saturated amount of pheno1 adsorbed into carbon sph巴res was determined aft巴1・keepingthe samp1e spheres in th巴pheno1 solution with a concen仕ationof 0.02 mo1/L for 24 h under st1rrmg at room temperature. In order to understand the m巴chanismof micropore formation in the very beginning of oxidation, the

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a reference temperatur巴of400 oC for th巴oxidationin the present activation condition (企yair with a flow rate of 50 mL/min) was possib1e to be obtained by shifting th巴 experimenta1 points at each oxidation temperature a10ng the abscissa (logarithm of oxidation time) to b巴consistentwith the points m巴asuredat 400 oC (Fig. 1 b)ー P10t of shift factors against the inverse of oxidation temp巴ra旬r巴(A立heniusp1ot) gave a linear re1ation, as shown in Fig. 1c, and its slope gave an apparent activation energy LiE of about 150 kJ/mol. In wet air, LiE of about 200 kJ/mo1 was obtained, as reported in our previous pap巴r14)

measurement of small ang1e X-ray scattering (SAXS) was carried out for carbon sph巴resslight1y oxidized. D巴tailsof

experimenta1 conditions were reported in our paperI7). The fundamenta1s on these t巴chniqueshave to be refe町巴dthe

respective origina1 papers27-29).

3.Air Activation Process

Masier Curve and Apparel1t Activation Energy 3.1 Oxidation yield

Oxidation yie1d is p10tted against oxidation tim巴for

different oxidation t巳mperaturesin Fig. 1a. Master curv巴at

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輔 叩 訓 容 器 費 髭 九 窓 必 h a e 四 百 唱 言 。 -1.5 0,居住14 10号 ti",.!h M W 10 0,,;謀説島民主irn_1需品 Fig. 1 Oxidation yie1d as白nctionsof oxidation tempera加reand tim巴. already a high va1u巴clos巴to600 m2/g even after 10 h oxidation at 400 oC. Intermediate oxidation temperatures resu1ted in int巴rmediate change in BET surfac巴area,as shown by dotted line for 400 oC in the figur巴 Thesame procedure as oxidation yie1d was applied to obtain th巴master curve at 400 oC for BET surface area (Fig. 2b). To cons廿uctthis mast巴rcurve, the same va1ues of shi日tfactors as thos巴usedfor oxidation yie1d were app1ied. 3目2BET sUlface area BET surface ar巴awas p10tted as functions of oxidation temperature and time in Fig. 2a. BET surface area obtained at 355 oC incr回目巴d slight1y企om about 400 m2/g with increasing oxidation time. At the highest t巴mperatureof 430 ocヲ BET surfac巴 areaquick1y increas巴d after 30 h oxidation but then decreased with increasing oxidation time. Howev巴r,it has to b巴pointedout that BET surfac巴areawas

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mtl搬 を!ft 司 1 1制2 Oxidatio岨time/l! 10 唖 Fig. 2 BET surfac巴areaas functions of oxidation temperatt江eand tim巴 yi巴1d巴drapid decrease in BET surfac巴area By the pr巴sentsimp1e oxidation in dry air, BET surfac巴 area abov巴 1000 m2/g cou1d be obtained by se1ecting appropriat巴conditions,about 30 h at 430 oc or about 65 h at 4000C ‘ 3.3αsplot anαlysis Even though there are some scattering of experimenta1 points, the master curve was ab1e to be obtain巴dusing the sam巴shi白血gprocedure as oxidation yie1d, in other words,

conversion betw巴巴n oxidation temperature and time was

possib1e for BET surface area. BET surface area increased gradually in th巴 beginning of oxidation, followed by

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Four pore param巴ters,micropore volume, microporous

surfac巴area,巴xtemalsurface area and total surface ar巴a,

which were determined by αs plot analysis, were shown as master curves at 400 oC in Figs. 3a to 3dヲrespectlV巴ly. To construct these master curves, the same shift factors at each oxidation temperature as those for oxidation yield were used. Micropore volume and microporous surface ar巴a show巴da maximum, but extemal surface ar巴astarted to increase around 10 h oxidation and continued to increase by further oxidation, the former was much larger, by about one order of magnitude, than the la社巴rin the present samples.

Total surface area showed a maximum,αs BET surface ar巴a

volume 輔 I AUM H t ・2 制 b、 i 弘 伊也 a o - 部 噌 咽 A 法 舗 , o i 耳 、 , , d i 邑 告)Extcmal surfacc畠rca 5自 4唖 帽

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払 主計酔 did, because this is the sum of microporous and external surface areas The master curves on micropor巴s,l.e.ラ mlcropore volume (Fig. 3a) and microporous surface area (Fig. 3b), r巴vealthe formation of a large amount of micropores by the oxidation at 400 oC only1.5 h, giving about 0.2 m]jg of micropore volume and about 400 m2jg of microporous surface area. This experimental fact is du巴tothe opening of th巴closedpores which exist in the original glass-like carbon, as will be shown in th巴followingsection 4. b) iVlicroporOl.L'>品u!ぬむ哲也f佳品 12税} n u w s f “ 0 1 ! 10 i骨融 Odd損主主婦time!lu: d) Tutal surfac己出向品 120世 !I 1 1a 唖 1品。 Oxidatilln ti齢 世ihr Fig. 3 Master curves for different pore parameters obtain巴dbyαs plot analysis. 3.4DFT and BJH analyses On the same samples pore size distributions in micropores ranging from 0.4to 2 nm and mesopores from 2 to 50 nm was d巴terminedby using DFT and B丘"{methods, respectively目 From the cumulative pore volumes of resp巴ctivemethod, micropore and mesopor巴volumeswere

calculated for each samples and plott巴d as functions of

oxidation t巴mperatureandむm巴ー As w巴did for oxidation

yield, BET surface area and four pore parameters, the master curves at 400 oC for micropore and mesopores volumes wer巴

obtained, as shown in Fig. 4. Micropore volume was separated into two subclass巴s, ultramicropore and sup巴rmicropore,as shown only mast巴rcurves for each paramet巴r in Fig. 4a. On th巴 pore size distribution determined by B耳"{method, the pores with the size of above 5 nm size were negligibly small amount In the beginning of oxidation

micropore volum巴 increased gradually with incr巴asingoxidation time, which were supposed to be due to th巴increasein ultramicropore volume. Beyond 10 h oxidation, micropore volume increas巴drapidly, where ultramicropores d巴cr巴asedgradually and supermicropores incr巴as巴d, no development of mesopores above 2 nm yet. Beyond 30 h oxidation, mesopores seemed to be develop巴d,though the development of supermicropores was still continu巴d. After 50 h oxidation, how巴ver,micropore volume decreased rapidly with incr巴asingoxidation time (F沼田 4a),as microporous surface area did (Fig. 3b), but mesopore volume continued to increase (Fig. 4b), as巴xt巴rnalsurface紅 巳adid (Fig. 3c)

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idation松田cfllr OxidatIon ti 臨 企Ih Fig. 4 Mast巴rcurves for micropores and mesopores

4. Formati.on Mechanism of Micropores

In Fig. 5a, adsorptionldesorption isotherm of N2 gas at

77 K is shown for the carbon sph紅 白oxidizedfor 2.5, 20 and

75 h at 400 oC, each of which corresponds to the beginning of pore development, that of increasing micropore volume and that at the maximum in micropore volume, resp巴ctively,

as shown togeth巴rwith th巴isothermfor the original carbon

spheres in Fig. 4a. Adsorption ofN2 gas became mark巴dby

the oxidation at 400 oC for 2.5 h, with a pronounc巴d a) Adsorptionldesorption isotherm 400 35骨

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h : s 孟'"30唖 、庖地 25骨 400 "C for20討 differenc巴 企om the original spheres. This increase in adsorption was resulted from the increases in BET surface area合omfew to about 400 m2/g and in microporvolume measured by αs plot from almost zero to about 0.17 ml/g, as shown in Fig. 2a and 3a, resp巴ctively. With increasing oxidation time at 400 oC, the adsorbed amount of N2 gas increased and the isotherms observed change合omType 1 to Typ巴 II,suggesting th巴 mcrease m macropores企om micropore dominant solid b) POre size distribution by DFT analysis 0.7膏 0.6 」予告.5 w富a 、、札4 金必 4G00CM5h

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車.2 住町4 仏軍 Rel且ti¥'eprcs草笛re1'11'0 9 骨,5 1.5 2 2.5 p"間 帯iutbI民 間 Fig. 5 Adsorption/desorption isotherms and por巴sizedistributions for carbon spheres oxidized. Pore size distributions measur巴dby DFT analysis on the oxidized carbon spheres are shown in Fig. 5b. On the carbon spheres oxidized at 400 oC for 2.5 h, pores less than 0.4nm seemed to be predominant, 町 田thoughthese por巴S could not be measured, in other words, most of th巴pores exist巴doriginally in the carbon sph巴resw巴r巴notyet op巴ned and only the en仕anceshaving th巴SlZ巴lessthan 0.4nm were form巴d. After 20 h oxidation at 400 oC, th巴populationof the por巴s(openings of por巴s)with the size of around 0.6 and 1.2 nm increased and the total micropore volume incr巴ased 企omabout 0.17 ml/g to about 0.28 ml/g (Fig. 4a). The pore size distribution curv巴obs巴rvedon th巴sampleoxidized at 400 oC for 20 h suggested a high population of th巴pores smaller than 0.4nm, higher than th巴samplesoxidized for 2.5 h, suggesting that all por巴soriginally巴xistedin carbon sphere were not yet opened. By the oxidation for 75 h, the population of the pores smaller than 0.4nm became almost zero, in other words, all closed pores wer巴opened,and that

ofth巴poreswith the size of around 0.6 nm decr巴ased,but that of th巴poreswith1.2 nm size increased markedly. On this sampl巴,the presence of the pores with the size of about 0.9 nm was clearly observed. In the case of the sampl巴 oxidized for 20 h, there was also small population of the pores with almost the sam巴slze At 400 oC, the仕endto increas巴thevolum巴ofpores with the sizes of around 0.6 and 1.2 nm was clearly observed,

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and the pores less than 0目4nm seems to decrease. At 430 oc, the same trend could b巴 r巴cognized. After 75 h

oxidation at 430 oC (150 h at 400 oC),however, por巴volume

corresponding to the pores with 0.6 and 1.2 nm sizes decreased, probably because pores were wid巴n巴dto more

than 2 nm by oxidation.

Th巴results shown in Fig. 5b suggest巴dth巴gradual

change in pore size (the sizes of openings)企omless than 0.4 nm to 0.6 nm and then to 1.2 nm. The sam巴analysisby

DFT method on the samples oxidized at intermediate conditions, i.e., oxidation tim巴企om2.5 to 75 h at 400 oc, was supported this supposition based on Fig. 5b. On the sampl巴soxidized for more than 75 h at 400 oC, a rapid

d巴cr回目巴 inmicropore volume and a corresponding rapid

increase in mesopore volume was observed in Fig. 4. InFig. 6a, pore width d巴terminedfrom SAXS analysis was plott巴das functions of oxidation temperatur巴andtim巴. a) At different oxidation tempera旬r巴 5 400 "C 4 同 何 回

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今 3 ウ ん 阿 古 吉 区 O H O 仏 l h u 10 100 Oxidatioll time I h The pore width calculated was obtained by sub仕actingthe

contribution from the spaces among spheres and also closed pores existed in the original spheres, and so it was reasonably supposed to the average size of pores form巴dby oxidation.

Th巴porewidth measured increases rapidly with increasing

oxidation time at each oxidation temperature. The high巴r

oxidation temper的lregives th巴mcreas巴inpore width with

the shorter oxidation time, although the mesurements were r巳S仕ictedto the beginning of oxidation in order to discuss on the formation of miropor巴s. The experimental points measured at different temperatures could be shi食巴dalong th巴 abscissa, oxidation time in the logarit加nicscal巴,to deduc巴 the master curv巴at400 oC (Fig 6b). The shi自factorsfor each oxidation t巴mperaturewer巴 巴xactlythe sam巴asthos巴 used for oxidation yield in Fig. lc. The mast巴rcurve for

micropore width determin巴dthrough SAXS analysis was

also obtain巴d,as for different pore parameters b) Master curve at 400 oc 5 A 斗 ﹄

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10 Oxidatiol1time I h Fig. 6 Micropor巴widthdetermined through SAXS analysis as functions of oxidation t巴mp巴ratureand time.

The micropores formed in the carbon spheres had the average size of0.7~0.8 nm by the air oxidation at 400 oC for 2.5 h, grew slightly to about 1.0 nm after 10 h oxidation and then increased rapidly with increasing oxidation time. The pore size thus determined by SAXS analysis shows a good correspondence to that observed by gas adsorption with DFT analysis (Fig. 5b). Ther巴fore,the pores detected by SAXS ar巴supposedto the holes (openings) formed on the wall of pores originally exist巴din carbon sphere. This supposition seems to b巴consistentwith th巴resultthat pore size increases very rapidly (Fig. 6b). The present results obtained by N2 gas adsorption and SAXS may suggest that the principal process for the formation of micropores was the opening of the closed pores, which existed originally in the carbon sph巴res. 伝Adsorptionof phenol Adsorption of phenol企omits aqueous solution was saturated after 10 h, as an isotherm for th巴carbonspher巴s oxidized at 400 oc for 100 h was shown in Fig. 7a. For carbon spheres oxidized, ther巴fore,th巴saturatedamount of ph巴nol adsorbed was calculated企om the concen仕ation chang巴afterbeing kept for 24 h and plotted as functions of oxidation temperature and time in Fig. 7b. By the same procedure with the sam巴shiftfactors as those for oxidation yield, the master curv巴forphenol adsorption for the carbon spheres oxidized at 400 oC was obtained, as shown in Fig 7c Inorder to understand the corr巴spondence b巴tw巴巴n adsorptivity for phenol (saturated amount of phenol adsorbed) and pore structure of th巴oxidizedcarbon spheres,

adsorptivity measured was plotted against micropore volume obtained fromαs plot. As shown in Fig. 8a, no correspondence between these two parameters was observed. How巴V巴r,a good linear relation was obtained between

adsorptivity and the volume for utlramicropores, as shown in Fig.8b.

If the attention was paid to two special points indicated byキ1and *2 in Fig. 8a, which were obtained on the carbon

spheres oxidized at 430 oc for 10 and 75 h, respectively, micropore volume for these two spheres was not so much different, but their adsorptivity for ph巴nolwas quite different. The former contained a large amount of ul仕amicroporesbut in the latter only a small amount of ultramicropores was remained after long time oxidation, as shown in Fig. 8b, which resulted in a big difference in adso中tivityfor phenol. Adsorptivity values for these two pointsヰ1and *2 are on th巴 straight line plotted against ultramicropore volum巴(Fig.8b).

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21) 的 常雲 吋 Fig. 8 R巴1ationof pheno1 adsorptivity on micropore vo1ume. because these methods were based on thediffi巴r巴nt assumptions. However, re1ative changes in various por巴 parameters with time at a reference t巴mperatureare possib1巴 to b巴comparedusing th巴mastercurves with each other The master curve of BET surface area (Fig. 2b) is very simi1ar with that of microporous surfac巴ar目 白terminedby αs p10t (Fig. 3b), which is reasonab1e because BET surface area is govemed by th巴pr巴senceof micropores. Th巴former gav巴themaximum at about 65 h oxidation at 400 oC, but the 1atler at about 30 h oxidation, shifting to shorter oxidation time, which is reasonab1e by taking into a consid巴rationthat m巴soporesar巴a1socontribute to BET surfac巴area. The deve10pment of mesopores started from about 30 h oxidation (Fig. 4b). Extema1 surface area measured by αs p10t (Fig. 3c) has veηsimi1ar change with oxidation tim巴tothat of mesopore vo1ume (Fig. 4b). The master curves of micropor巴vo1umedetermined by αs p10t and DFT m巴thod (Fig. 3a and 4a, respective1y) are a1so simi1ar with each oth巴r to show a maximum as those for microporous surfac巴ar回 (Fig. 3b) and BET surface area (Fig. 2b). Maxima observed on BET, tota1 and microporous surface area (Fig. 2b, Fig. 3d and Fig. 3b, resp巴ctive1y)ヲ arereasonab1y und巴rstoodas a resu1t of the comp巴titionbetw巴巴nen1argem巴ntand collapse of pores and subs巴quentpore surface area 10ss. 6. Discussion The shift factors used in order to construct mater curves for not only oxidation yie1d but a1so various pore parameters and adsorptivity for pheno1 gave th巴 apparentactivation energy of about 150 kJ/mol. If we take into account of the fact that the formation巴n巴rgiesof CO2 and CO gases are about 394 and 111 kJ/mo1, r巴spective1y,th巴obtainedva1u巴of apparent activation energy is in between these two formation energies. In wet air, the apparent activation energy of about 200 kJ/mo1 was obtained14lー The activation四 巴rgy determined h巴reis on1y apparent va1u巴 inother words, a1temative expression of the conversion factors between tempera旬reand time for oxidation. In th巴presentwork, therefore, the discussion to compare the prese凶 activation energy va1ues with those r巴portedon the basis on the kinetic studies of oxidation and gasification of various carbon mat巴ria1s was not carried ou.t The va1ue of activation

energy obtain巴d by the present shifting proc巴dure is supposed to depend on the particle size and morpho1ogy, as well as oxidation conditions, such as oxidizing agent and its conc巴ntrationand flow rate,巴tc It has to be pointed out her巴thatth巴comparisonamong the abso1ute va1ues of pore paramet巴rs,which were determined by different m巴thodsof ana1ysis, was difficu1t

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h w 説 明 州 諸 制 同 同 時 一 両 点 . ‘ 留思岡. .

a

d 勾e' ー ‘-、 担 o 寝耳p 1 10 100 Oxidatio盟timc/ b Fig. 9 Dev巴10pmentof pores in carbon spheres through air oxidation. InFig. 9, master curves for micropore vo1um巴 determined by αsp10t, u1tramicropor巴andsupermicropore vo1umes by DFT method and mesopore vo1ume by BJH method are reproduced in order to malce the comparison easier, together with some SEM註nages to show the appearance of sphere. Inthe beginning of oxidation, i.e., up to 10 h oxidation at 400 oC, th巴mainprocess is the formation of u1仕amlcropor巴, main1y due to opening of closed pores existed originally in glass制likecarbon nanotexture. Above 10 h up to about 60 h, re1ative amount of u1位amicropores form巴d decreas巴d but supermicropores increase with increasing oxidation time. Above 65 h, micropores ( a sum of u1tra- and super-micropores) decreased rapid1y but mesopore vo1ume incr巴asedslight1y, which resu1ted in the decrease in surface areas measured by different methods. This change in pore vo1umes may suggest the op巴ningof c10sed pores to form ultramicropores, followed by the gradua1 en1argement and collapse of pores from u1tramicropore to macropore through supermicropore and mesopore. SEM obs巴rvationof sphere surface seems to agree with this pore deve10pment sequence, as shown in Fig. 9, and it gives some information on macropores, which cou1d not be measured through the gas adsorption ana1yses. After few hours oxidation, no change on the surface of sphere was detected because micropores cou1d not be seen under SEM. After around 20 h oxidation on1yfi巴w pit同likeho1es w巴r巴 observ巴d,wher巳 supermicropores and mesopores wer巴 supposed to be deve10ped. Around and after passing through the maximum of micropore vo1ume, the surfac巴of spheres b巴camerough du巴tothe formation of macropores on the surface To understand the oxidation reactions企omthe vi巴W point of gasification, it was proposed to normalize the 企actiona1 burn-off in different atrnospher巴s ( different oxidizing agents, such as O2, steam and CO,z and th巴lr different pressures) as a function of tltO.5, where tO.5 is the time giving企actiona1bum-off of 0.528). The exp巴rimenta1 data of bum-off obtained at a constant tempera札lrefor each oxidizing agent were successfully unified to one curve. This ana1ysis procedure was used for the ana1ysis of gasification r巴action of chars29,30), and a1so successfully appli巴dto the data measured at different temperatures31) to get so-called“unification curv巴s", Unification curves obtain巴dare expressed as a function of dimensionl巴sstime t/t0.5, but master curves derived in the pres巴ntwork are巴xpressedby rea1 time at a reference

t巴mpera旬r巴 Theformer seems to be usefu1 to compare the

gasification of various carbonac巴ousmat巴ria1sand to discuss its mechanism, but the 1att巴rmay usefu1 to discuss the activation conditions to pr叩 紅 白activatedcarbons. 7. Conclll.sion Pores were d巴ve10ped in carbon spher巴s by the oxidation in drγair. Th巴 deve10pment of pores was und巴,rstoodby the master curves for each pore parameters, in other wordsラth巴conversionbetween oxidation temperature and time was possib1e for pore deve10pment for the oxidation at a tempera旬rebetw巴en355 and 430 oC in a f10w of dry air. Pored巴ve10pmentwas supposed to be proceeded principally the opening of closed pores巴xistedoriginally in glass-like carbon nanotexture to form ultramicroporesラfollowedby the collapse and en1argement of u1tramicropore to macropore through supermicropor巴andmesopore. Aclmowledgement

The present work was part1y supported by a grant of the Frontier R巴s巴archProject "Materia1s for the 21st Century

句Materia1s D巴ve10pment for Enviromnent, Energy and Information-"企omMinistrγof Education, Cu1ture, Sports,

Science and Techno1ogy. The authors wou1d like to express their sincere thanks to Profs.K. Nishikawa of Chiba

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University, K.Oshida of Nagano Nationa1‘Colleg巴 of Techno1ogy and K. Fukuyama of M吋iGakuin Universi句r and Dr.K. Hatakeyama of Chiba University for th巴ir cooperation and encouragement. References T.D. Burchell, Ed. (1999) Carbon Materiαlsfor Advanced Technologies, Pergamon 2 M. Inagaki (2000) New Carbons -Control in structure and

nctions-,E1sevier 3 M. Inagaki and F. Kang (2006) Carbon Materials Science and Engineerng -From Fundamentals to Applications-, Tsinghua Univ. Press 4 Y目Sanada,M.S回 出i,K.Fujimoto, Ed. (1992) Activated Carbons -Fundamentals and Applications-, Kodansha Sci. 5 F. Rodrigez-Reinoso, lntroduction to Carbon Technologies, Marsh HラH巴intzEA, F .Rodrigez -Reinoso Ed., Univ. de A1icante, p. 35-101 (1997). 6 F. DerbyshireラM.Jagtoyen, M. Thwaites. Activated Carbons -Production and Application. In:J.W. Patrick Ed., Porosity in Carbons, Edward Arno1d (1995) 227-252. 7 M. Inagaki and M. Nakashima, Tanso, 1994 [No.162] 61-65 (1994). 8 M. Inagaki and M. Sunahara, Tanso, 1998[No.183] 146-150 (1998). 9 M.1.Kim, C.H.Yun, Y.J.Kim, C.R. Park and M. Inagaki, Carbon, 40, 2003凶2012(2002) 10 M.Inagaki, M.Sunahara A.Shindo, V.Vigna1 and H.Konno

JMater.Res., 14

3208-3210 (1999). 11 V. Vigna1, A.MorawskiぅH.Konno and M. Inagaki, J Mater. Res., 14

1102-1112 (1999).

12 M. Inagaki, V. Vigna1, H. Konno and A.Morawski, J Mater. Res., 14

3152-3157 (1999).

13 M. Inagaki, E. Bourelle, V. Vigna1, H. Konno, A.W. Morawski, Synth. Met., 125ラ231-238(2002)目 14 M. Inagaki and T. Suwa, Mol. Cryst.Liq. Cryst. 386

197 (2002) 15 Y. J.Kim, M. 1.Kim, C. H. Yun, J. Y. ChangヲC.R Park and M. Inagaki, J Colloid lnte宅向ceSci. 274, 555-562 (2004) 16 T. Nishikawa and M. Inagaki, Ads. SCI. Tech. 23, 827-837 (2005).

17 M. Inagaki, T. Nishikawa, K.Oshida, K. Fukuyama,Y. Hatakeyama and K.Nishikawa, Ads. Sci. Tech., 24, 55-64 (2006) 18 M. Inagaki and M. Nakashima, Cαrbon, 30 1135-1136 (1992). 19 M. Nakashima, S. Shimada, M. Inagaki and T. A Centeno

Carbon, 33

1301-1306 (1995) 20 O. Tanaike, M. Fukuoka and M. Inagaki,伽7th.Met., 125,255守257(2002) 21 A.W目Morawskiand M. Inagaki, Desalination, 114 23-27 (1997). 22 A.W. Morawski, R. Ka1enczuk and M. Inagaki, Desalination, 130, 107-112 (2000)目 23 M. Inagaki and M. Sakanishi, AdsorptIon SCI. Tech., 21, 587-595 (2003) 24 M. ToyodaラY.Nanbu, T. Kito,為1.Hirano and M. Inagaki, Desalination, 159ヲ273-282(2003) 25 J.M. Skowronski and M. Inagaki, Karbo, 2002,ふ11 (2002) 26 L. Wang, M, Fujita and M. Inagaki, Electrochimca Acta, 51,4096-4102 (2006)

27 L. Wang and M. Inagaki, New Carbon Mater. (in press).

28

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M. P. Mah勾an,R. Yarzab, P. L. Wallar J,.rFue1, 57, 643 (1978).

29 S. Kasaoka, Y. Sakata, and C. Tong, lntl. Chem. Eng., 25, 160 (1985).

30 F.F.P巴ng,1. C. Lee, R. Y. K.Yang, Proc. 3rd

Pittsburgh Coal Confヲp.730. (1986)

31 K. Raghumathan, R.Y. K. Yang,lnd.Eng. Chem. Res., 28,518 (1989)ー

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