ºîÀ®¡§ 1998/10/30 ¿ÜÆ£¡¡¹â»Ë
¥Ç¡¼¥¿Èֹ桡¡¡¡¡¡§010123
´Ä¶±øÀ÷ʪ¼Á¤ÎÅÅ»ÒÀþ½èÍýÍøÍѤˤª¤±¤ëºÇ¶á¤Î¿ÊŸ
ÌÜŪ¡¡¡¡¡¡¡¡¡¡¡¡¡§±øÀ÷Ãϲ¼¿å¤ÎÅÅ»ÒÀþ¾È¼Í½èÍýË¡¤Î³«È¯
Êü¼ÍÀþ¤Î¼ïÊÌ¡¡¡¡¡§ÅÅ»Ò
Êü¼ÍÀþ¸»¡¡¡¡¡¡¡¡¡§ÅŻҲî´ï (1MeV¡¢50mA¡¢75kW)¡¢ÅŻҲî´ï (500keV¡¢40mA¡¢25kW)
¥Õ¥ë¥¨¥ó¥¹¡ÊΨ¡Ë¡§0-5 kGy¡¢0-163 kGy
ÍøÍÑ»ÜÀß̾¡¡¡¡¡¡¡§The Electron Beam Research Facility (EBRF)
¾È¼Í¾ò·ï¡¡¡¡¡¡¡¡¡§Â絤Ãæ
±þÍÑʬÌî¡¡¡¡¡¡¡¡¡§¥Ï¥í¥óʬ²ò¡¢Íµ¡±øÀ÷¿å¤Î̵³²²½
³µÍס¡¡¡¡¡¡¡¡¡¡¡¡§
¡¡¿åÍϱդËÅÅ»ÒÀþ¤ò¾È¼Í¤¹¤ë¤È¿ô¼ï¤Î³èÀ¼ï(¥é¥¸¥«¥ë¤ä¥¤¥ª¥óÅù)¤òÀ¸¤¸¡¢¤½¤Î³èÀ¼ï¤¬¿å¤ËÍϤ±¤¿Íµ¡Í³²Êª¤ÈÈ¿±þ¤·¡¢¤³¤ì¤é¤òʬ²ò¤¹¤ë¡£³èÀ¼ï¤ÎÀ¸À®È¿±þ¤ÎGÃͤä³èÀ¼ï¤È͵¡Êª¤È¤ÎÈ¿±þ¤Î®ÅÙ¤òÆþÎϤ·¡¢Æ°ÎϳØŪ¥â¥Ç¥ë¤òºîÀ®¤·¡¢¼Â¸³·ë²Ì¤È¤ÎÈæ³Ó¤ò¹Ô¤Ã¤¿¡£Îɤ¤°ìÃפòÆÀ¤¿¤¬¡¢¼ÂÍѲ½¤Ë¤Ï¹¹¤Ë¸¦µæ¤¬É¬ÍפǤ¢¤ë¡£Êƹñ¤Ç¤Î¹¥·ë²Ì¤ò´ð¤Ë¡¢°ÜÆ°¼°ÅÅ»ÒÀþ½èÍýÁõÃ֤ˤè¤ê¡¢ÆȤˤª¤¤¤Æ³Æ¼ï±øÀ÷¿å¤Î¾È¼Í¼Â¸³¤ò¹Ô¤¤¡¢´û¸ÁõÃ֤ȷкÑŪ¤Ë¤â¶¥Áè¤Ç¤¤ë¤³¤È¤ò³Î¤«¤á¤¿¡£
¾ÜºÙÀâÌÀ¡¡¡¡¡¡¡¡¡§
¡¡
¡¡±øÀ÷ʪ¼Á¤Î¿åÍϱդËÅÅ»ÒÀþ¾È¼Í¤ò¹Ô¤¦¤È¡¢´Ô¸µÀ¿åÏÂÅŻҡ¢¿åÁǸ¶»Ò¡¢»À²½À¿å»À´ð¤ò´Þ¤àÈó¾ï¤ËÈ¿±þÀ¸¤Î¹â¤¤³èÀ¼ï¤òÀ¸¤¸¤ë¡£¤³¤ì¤é¤¬Íµ¡ÍϼÁ¤ËºîÍѤ·°ìÏ¢¤ÎÈ¿±þ¤òµ¯¤³¤·¡¢±øÀ÷ʪ¼Áʬ»Ò¤òʬ²ò¤¹¤ë¡£ËÜÊó¹ð¤Ç¤Ï¡¢Íµ¡²½¹çʪ¤Î½üµî¤ÎÆ°ÎϳØŪ¥â¥Ç¥ê¥ó¥°¤È°ÜÆ°¼°ÅÅ»ÒÀþ½èÍýÁõÃ֤ˤè¤ë±øÀ÷¿å¤«¤é¤Îͳ²Êª¼Á½üµî¤Î»î¸³¤Ë¤Ä¤¤¤Æ½Ò¤Ù¤ë¡£¡¡
¡¡
¡¡¿å¤ÎÅÅ»ÒÀþ¾È¼Í¤Ë¤è¤ê¿ô¼ï¤Î¥é¥¸¥«¥ë¡¢¥¤¥ª¥ó¡¢¤Èʬ»Ò¤¬À¸¤¸¤ë¡£¡¡
¡¡
H2O+ÅÅ»ÒÀþ¢ª[2.6]eaq- + [0.6]H¡¦ + [2.7]OH¡¦+ [0.45]H2 + [0.7]H2O2 + [2.7]H3O+¡¡¡¡(1)¡¡
¡¡¹â¥¨¥Í¥ë¥®¡¼ÅŻҤ¬¿åÍϱդòÄ̲ᤷ¤Æ10-7Éøå¤Î¿åÃæ¤Ç¤ÎÈ¿±þ¤ò¼¨¤¹¡£[ ] ¤Î¿ôÃͤÏGÃͤǤ¢¤ë¡£
¡¡
¡¡À¸À®¤·¤¿3¼ï¤Î³èÀ¼ï¡¿¥é¥¸¥«¥ë¤Ï¤ª¸ß¤¤¤Ç¤âÈ¿±þ¤¹¤ë¤¬¡¢¿å¤Ë´Þ¤Þ¤ì¤ë¾¤Î¥¤¥ª¥ó¤äÍϼÁ¤ÈÈ¿±þ¤¹¤ë¡£½ã¿åÃæ¤Ç¤Î´ûÃΤÎÈ¿±þ¤ËÃϲ¼¿å½èÍý¤Ç¤ÎÍϼÁ¤È¤ÎÈ¿±þ¤ò²Ã¤¨¤Æ¡¢¤½¤ì¤é¤ÎÈ¿±þ®ÅÙ¤òÆ°Îϳإâ¥Ç¥ë¤ËÆþÎϤ¹¤ë¡£¤³¤ì¤é³èÀ¼ï¤Î½é´üÇ»Å٤ϾȼÍÎ̤«¤é(1)¼°¤ÎGÃͤè¤êÆÀ¤é¤ì¤ë¡£OH-¤ÈH+¤Î¥¤¥ª¥óÇ»ÅÙ¤ÏpH¤Ç¡¢¤Þ¤¿Ãº»À¤È½Åú»À¥¤¥ª¥óÇ»ÅÙ¤ÏÁí¥¢¥ë¥«¥êÀÅÙ¤ÈpH¤«¤é·×»»¤µ¤ì¤ë¡£³Æ¼Â¸³¤Ë¤ª¤¤¤ÆpH¡¢Áí¥¢¥ë¥«¥êÀÅÙ¡¢Íϲò»ÀÁÇ¡¢Íϲò͵¡ÃºÁÇ¡¢¾Ë»À±ö¥¤¥ª¥óÇ»ÅÙ¤ò·×¬¤·¡¢Æ°Îϳإâ¥Ç¥ë¤Î½é´ü²½¤ò¹Ô¤¦¡£Ãϲ¼¿å½èÍý¤ÎÁ´¤Æ¤ÎÈ¿±þ¤È¤½¤ÎÈ¿±þ®ÅÙ¤ÏRoss¤Î¾È¼ÍÆ°Îϳإǡ¼¥¿¥Ù¡¼¥¹¤«¤éºÎÍѤ·¤¿¡£Ëܸ¦µæ¤Ç»ÈÍѤ·¤¿ÍϼÁ½üµî¤ÎÈ¿±þ¤òɽ1¤Ë¼¨¤¹¡£
ɽ1¡¡Reactions and rate constants for destruction of carbon tetrachloride, chloroform and methylene chloride.¡Ê¸¶ÏÀʸ1¤è¤ê°úÍÑ¡Ë
Carbon tetrachloride k(M-1s-1) References
CCl4+ eaq- ¢ªCCl3+Cl- 1.3¡ß1010 Afanassiev et al.,1979
CCl4+H ¢ª CCl3+Cl-+H+ 3.2¡ß107 Koester et al.,1971
CCl3+O2 ¢ª products 3.3¡ß109 Moenig et al.,1983
CCl3+CCl3 ¢ª products 3.7¡ß108 Lesigne et al.,1974
¡¡ËÜɽ¤ÎÈ¿±þ®ÅÙ¤«¤éÃíÌܤÎÍϼÁ¤Îʬ²ò¤Ë´óÍ¿¤¹¤ëÏ¢º¿È¿±þ¤Î¤¤Ã¤«¤±¤È¤·¤Æ¡¢¿åÏÂÅŻҤ¬½ÅÍפʳèÀ¼ï¤Ç¤¢¤ë¤È»×¤ï¤ì¤ë¡£¤Þ¤¿¿åÃæ¤ÎÍϲò»ÀÁǤâ½üµî¸ú²Ì¤Ë½ÅÍפÊÌò³ä¤ò̳¤á¤ë¡£¿å¾È¼Í¤Î·ë²Ìͽ¬¤ËÍ¥¤ì¤Æ¤¤¤ëAEC¤ÎMAKSIMA-CHEMIST¥³¡¼¥É¤ËÆ°Îϳإâ¥Ç¥ë¤òÆþ¤ì¤¿¡£Àµ¤·¤¤È¿±þ®Å٤Ǥ¢¤é¤æ¤ëÈ¿±þ¤òÁȤ߹þ¤ß¡¢Àµ³Î¤Ë¬Äꤵ¤ì¤¿Íϲò¥¤¥ª¥óÇ»Å٤δð¤Çͽ¬ÀºÅ٤ϸþ¾å¤¹¤ë¡£»Í±ö²½ÃºÁǤνüµî»î¸³¤òÇ»ÅÙ¤ª¤è¤ÓpH¤òÊѤ¨¤Æ¹Ô¤Ã¤¿¡£
¡¡
¡¡ÅŻҲî´ï¤ÏEBRF¤Î75kW¡¢1MeV¡¢50mA¤Ç¤¢¤ë¡£1¤È5¦ÌM¤Ç¤Ï½üµîGÃͤÏÊѤï¤é¤Ê¤¤¤¬¡¢¹âÇ»ÅÙ¤Î50¦ÌM¤Ç¤ÏGÃͤÏÄ㤯¤Ê¤ê¡¢½êÄê¤Î½üµîΨ¤òÆÀ¤ë¤¿¤á¤Î¾È¼ÍÎ̤Ϲ⤯¤Ê¤Ã¤¿¡£pH5-9¤Î¼Â¸³·ë¤Ç¤Ï¡¢»Í±ö²½ÃºÁǤνüµîÀǽ¤Ë¤ÏÂ礤ʱƶÁ¤Ï¤Ê¤«¤Ã¤¿¡£Áí¥¢¥ë¥«¥êÀÅÙ¤Ï0-60 mg/l¤Ç¡¢pH 9¤Ç¤Ïú»À¡¿½Åú»À¥¤¥ª¥óÈæ¤Ï0.25¡¢°ìÊýpH 7¤Ç¤Ï¤Û¤È¤ó¤É½Åú»À¥¤¥ª¥ó¤Ç¤¢¤ê¡¢pH5¤Ç¤ÏÆó»À²½ÃºÁǤǤ¢¤ë¤¬¡¢Ëܼ¸³¤Ç¤Ï¿å¤ò¤«¤º®¤¼¤¿¤Î¤Ç¾Ã»¶¤·¤¿¡£¤³¤ì¤Ë¤è¤ê¡¢Â¾¤Î¸¦µæ·ë²Ì¤È°Û¤Ê¤ë·ë²Ì¤È¤Ê¤Ã¤¿¡£¤³¤ì¤é¤Î¼Â¸³¤È·×»»¥³¡¼¥É·ë²Ì¤ÎÈæ³Ó¤òɽ2¤Ë¼¨¤¹¡£
ɽ2¡¡Experimental vs. model predictions of carbon tetrachloride removal (%) from 100 ¦Ìgl-1 influent solution.¡Ê¸¶ÏÀʸ1¤è¤ê°úÍÑ¡Ë
-----------------------------------------------------------
pH Dose,krad (%Removed)expt (%Removed)model Error,%
-----------------------------------------------------------
5 100 91 90 1
200 97 99 -2
300 99 100 -1
7 100 72 79 -7
200 97 96 1
300 98 99 -1
9 100 71 71 0
200 93 99 -6
300 96 100 -4
-----------------------------------------------------------
¡¡Ç»ÅÙ¤¬¾å¤¬¤ë¤È99%½üµî¤ËɬÍפÊÀþÎ̤â¾å¤¬¤Ã¤Æ¤ª¤ê¡¢·×»»·ë²Ì¤âÎɤ¤°ìÃפò¼¨¤·¤¿¡£º¹¤¬Éé¤Ë¤Ê¤Ã¤¿¤Î¤Ï¡¢¤ä¤ä·×»»¤¬½üµîΨ¤ò¹â¤¯¿äÄꤹ¤ë¤³¤È¤ò¼¨¤¹¡£Ëܻ¤Ï¼Â¸³¼¼´Ä¶¤Ç¡¢À©¸æ¤µ¤ì¤¿¾ò·ï¤Ç¹Ô¤Ã¤Æ¤ª¤ê¡¢¸½¼Â¤Î²¼¿å¤ä±øÀ÷Ãϲ¼¿å¤È¤Ï°Û¤Ê¤ë¤³¤È¤Ïʬ¤«¤Ã¤Æ¤ª¤ê¡¢¹¹¤Ë¸¦µæ¤ò¿¼¤á¤ë»ö¤¬É¬ÍפǤ¢¤ë¡£
¡¡
¡¡ºÇ½é¤Î²°³°¼Â¸³¤Ï1994ǯ½©¤Ë»°±ö²½¤ª¤è¤Ó»Í±ö²½¥¨¥Á¥ì¥ó¤Ç±øÀ÷¤µ¤ì¤¿Ãϲ¼¿å¡¢Î®ÎÌ20GPM¤Ç¹Ô¤ï¤ì¤¿¡£¤³¤Î¼Â¸³¤¬À®¸ù¤Ç¤¢¤Ã¤¿¤Î¤Ç¡¢µ»½Ñ°Üž¤Î¤¿¤á¡¢°ÜÆ°¼°ÅÅ»ÒÀþ½èÍýÁõÃÖ¤òÆȤØÁ÷¤ê¼Â¸³¤·¤¿¡£ÅÅ»ÒÀþ¤ª¤è¤ÓÊä½õÁõÃÖ¤Ï48¥Õ¥£¡¼¥È¤Î¥È¥ì¡¼¥é¤ËÀѤޤ졢ÅŸ»¤ä¼×ÊäòÈ÷¤¨¤Æ¡¢50 GPM¤Þ¤Ç¤Î½èÍý¤¬¹Ô¤¨¤ë¡£1m3¤Î¥µ¥ó¥×¥ë¿å¤¬¥È¥ì¡¼¥é¤Ë±¿¤Ð¤ì¡¢½èÍý»ÜÀßÆâ¤ò50-199ʬ´Ö½Û´Ä¤¹¤ë¡£¼Â¸³¤Ç¤ÎήÎ̤ǡ¢3-14²ó¤Î¾È¼Í¤¬·«¤êÊÖ¤µ¤ì¤ë¤³¤È¤Ë¤Ê¤ë¡£ÅŻҲî´ï¤Ï25 kW¡¢500 keV¡¢40 mA¤Ç¤¢¤ê¡¢Á´½ÐÎϤǤμ¸³¤ò¹Ô¤Ã¤¿¡£¤½¤Î·ë²Ì¤òɽ3¤Ë¼¨¤¹¡£
ɽ3¡¡Summary of Electron Beam Removal of Various Organic Compounds from Refinery Process Water.¡Ê¸¶ÏÀʸ1¤è¤ê°úÍÑ¡Ë
-------------------------------------------------------------
Overall
Zero %
Analyte Dose 0.7 1.4 2.8 Removal
Mrad Mrad Mrad
-------------------------------------------------------------
ôPhenol ¦ÌgL-1 2230 220 60 20 99.10
Benzene ¦ÌgL-1 6200 150 10 3.5 99.95
Toluene ¦ÌgL-1 498 9 <1 BMDL >99.9
Ethylbenzene ¦ÌgL-1 118 2 BMDL BMDL >99.9
m/p-Xylene ¦ÌgL-1 201 4 <1 BMDL >99.9
o-Xylene ¦ÌgL-1 108 2 BMDL BMDL >99.9
ôAromatics ¦ÌgL-1 7125 167 10 3.5 99.95
Naphthalene ngL-1 15207 <20 >99.87
Fluorene ngL-1 728 <20 >97.25
Phenanthrene ngL-1 48 <10 >79.17
Anthracene ngL-1 138 <10 >92.75
Pyrene ngL-1 56 BMDL >99
Benzo-(a)-
anthracene ngL-1 12 BMDL >99
Fluroanthene ngL-1 86 <10 >88.37
ôPAH ngL-1 16277 BMDL >99.99
-------------------------------------------------------------
BMDL=below method detection limit.
¡¡¤³¤Î¾¤Ë¤â¡¢ÇÑ´þʪËäΩÃϤÎßɲá¿å¡¢»º¶ÈÇÑ¿å¤ä²þÁ±¤òÍפ¹¤ë¹©¾ìÍÑÃÏÃϲ¼¿åÅù¤Îͳ²Êª½üµî¼Â¸³¤ò¹Ô¤¤¡¢ËÜË¡¤¬½¾Íèµ»½Ñ¤È·ÐºÑŪ¤Ë¶¥Áè¤Ç¤¤ë¿·¤·¤¤µ»½Ñ¤Ç¤¢¤ë¤³¤È¤¬Ê¬¤«¤Ã¤¿¡£
¥³¥á¥ó¥È¡¡¡¡¡¡¡¡¡§
¡¡ÇÑ¿å¡¢¾å²¼¿å¤ÎÊü¼ÍÀþ½èÍý¤Ï¿§¡¹¤Ê¹ñ¤Ç¼Â¸³¤¬»î¤ß¤é¤ì¤Æ¤ª¤ê¡¢¼Â¸³¼¼Åª¤Ë¤Ï¤½¤Î͸úÀ¤¬Ç§¤á¤é¤ì¤Æ¤¤¤ë¡£¤³¤³¤Ç¤Ï¥Ñ¥¤¥í¥Ã¥ÈÁõÃ֤ǡ¢¼ÂºÝ¤Î¿å½èÍý¤ò¹Ô¤Ã¤Æ¤ª¤ê¡¢¤½¤ÎÍ¥°ÌÀ¤ò¼¨¤·¤¿¡£ÅÚ¾í±øÀ÷¤¬º£¸åÌäÂê¤È¤Ê¤ê¡¢¤½¤Î½èÍý¤È¤·¤Æ¤â¡¢ËÜÊýË¡¤ÏÍÍѤȻפï¤ì¤ë¡£
¸¶ÏÀʸ£± Data source 1¡§
Recent Advances in the Application of Electron Beam Processing to Pollution Control
Cooper, William J., Zele, Sarita R., Waite, Thomas D.*, Kurucz, Charles N.*, Kajdi, David C.**, Nickelsen, Michael G.**
Drinking Water Research Center, Florida International University, *University of Maiami,**High Voltage Environmental Applications Inc.
Âè22²óÆüËÜ¥¢¥¤¥½¥È¡¼¥×¡¦Êü¼ÍÀþÁí¹ç²ñµÄÏÀʸ½¸,P.341-355,1996
¥¡¼¥ï¡¼¥É¡§ÅÅ»ÒÀþ,͵¡±øÀ÷¿å,Êü¼ÍÀþʬ²ò,Æ°Îϳإâ¥Ç¥ë,È¿±þ®ÅÙ
electron beam, organic contaminated water, radiation decomposition, kinetic model, rate of reaction
ʬÎॳ¡¼¥É¡§010502,010505