华南理工大学学报(自然科学版)
華南理工大學學報(自然科學版)
화남리공대학학보(자연과학판)
JOURNAL OF SOUTH CHINA UNIVERSITY OF TECHNOLOGY(NATURAL SCIENCE EDITION)
2014年
2期
14-20
,共7页
李军%何水淋%李智%徐峻%莫立焕
李軍%何水淋%李智%徐峻%莫立煥
리군%하수림%리지%서준%막립환
蔗渣浆%ECF短序漂白%二氧化氯脱木素%过氧化氢强化氧脱木素%可吸附有机卤化物%直接化学品成本
蔗渣漿%ECF短序漂白%二氧化氯脫木素%過氧化氫彊化氧脫木素%可吸附有機滷化物%直接化學品成本
자사장%ECF단서표백%이양화록탈목소%과양화경강화양탈목소%가흡부유궤서화물%직접화학품성본
bagasse pulp%ECF short-sequence bleaching%chlorine dioxide delignification%peroxide-reinforced oxy-gen delignification%absorbable organic halide%direct chemical cost
对典型的蔗渣浆无元素氯(ECF)短序漂白流程D0 EpD、OpDEp及OpD进行了对比,探讨了二氧化氯脱木素(D0)与过氧化氢强化氧脱木素(Op )的脱木素效率差异及对后续漂白的影响,并分析了漂白过程中可吸附有机卤化物(AOX)的产生量和各漂白流程的直接化学品成本.结果表明:D0段脱木素选择性好,ClO2用量为0.8%时脱木素率即达40%以上,且用量越高脱木素作用越强;Op段在脱出纸浆中残余木素的同时能大幅提升纸浆白度,纸浆白度明显高于D0浆;相同后续漂白化学品用量下,OpDEp漂后浆白度高于D0EpD漂后浆白度,且比OpD漂后浆白度约高12个百分点;相同纸浆白度下,OpDEp漂白过程中产生的可吸附有机卤化物总量约为D0 EpD的50%,其直接化学品成本比后者低约40.00元/t,具有更好的环境、经济效益.
對典型的蔗渣漿無元素氯(ECF)短序漂白流程D0 EpD、OpDEp及OpD進行瞭對比,探討瞭二氧化氯脫木素(D0)與過氧化氫彊化氧脫木素(Op )的脫木素效率差異及對後續漂白的影響,併分析瞭漂白過程中可吸附有機滷化物(AOX)的產生量和各漂白流程的直接化學品成本.結果錶明:D0段脫木素選擇性好,ClO2用量為0.8%時脫木素率即達40%以上,且用量越高脫木素作用越彊;Op段在脫齣紙漿中殘餘木素的同時能大幅提升紙漿白度,紙漿白度明顯高于D0漿;相同後續漂白化學品用量下,OpDEp漂後漿白度高于D0EpD漂後漿白度,且比OpD漂後漿白度約高12箇百分點;相同紙漿白度下,OpDEp漂白過程中產生的可吸附有機滷化物總量約為D0 EpD的50%,其直接化學品成本比後者低約40.00元/t,具有更好的環境、經濟效益.
대전형적자사장무원소록(ECF)단서표백류정D0 EpD、OpDEp급OpD진행료대비,탐토료이양화록탈목소(D0)여과양화경강화양탈목소(Op )적탈목소효솔차이급대후속표백적영향,병분석료표백과정중가흡부유궤서화물(AOX)적산생량화각표백류정적직접화학품성본.결과표명:D0단탈목소선택성호,ClO2용량위0.8%시탈목소솔즉체40%이상,차용량월고탈목소작용월강;Op단재탈출지장중잔여목소적동시능대폭제승지장백도,지장백도명현고우D0장;상동후속표백화학품용량하,OpDEp표후장백도고우D0EpD표후장백도,차비OpD표후장백도약고12개백분점;상동지장백도하,OpDEp표백과정중산생적가흡부유궤서화물총량약위D0 EpD적50%,기직접화학품성본비후자저약40.00원/t,구유경호적배경、경제효익.
In this paper,first,three typical element chlorine-free (ECF)short-sequence bleaching processes, namely D0 EpD,OpDEp and OpD,were comparatively investigated.Then,the difference in delignification rate be-tween the chlorine dioxide delignification (D0 )and the peroxide-reinforced oxygen delignification (Op )was re-vealed,and the effect of pre-delignification on the subsequent bleaching was analyzed.Finally,the AOX (Absor-bable Organic Halides)emission and the direct chemical cost during the bleaching were discussed.The results in-dicate that (1 )D0 possesses high delignification selectivity;for instance,the delignification rate reaches 40%at a ClO2 dosage of only 0.8%and continuously increases with ClO2 dosage;(2)Op can not only delignify the residual lignin in pulp but also remarkably improve the pulp brightness to a value much higher than that of D0 pulp;(3 ) OpDEp bleaching is more effective than D0 EpD bleaching at the same chemical dosage in the subsequent bleaching because it may result in higher pulp brightness;(4)the final brightness of OpDEp bleached pulp is about 12 per-centage points higher than that of OpD bleached pulp;and (5 )at the same pulp brightness,the AOX emitted du-ring the OpDEp bleaching is only about half of that emitted during the D0 EpD bleaching,and the direct chemical cost of OpDEp bleached pulp is 40.00 Yuan/t lower than that of D0 EpD bleached pulp,which means that OpDEp bleaching is of higher environmental and economic benefits.