中国环境科学
中國環境科學
중국배경과학
CHINA ENVIRONMENTAL SCIENCE
2014年
5期
1200-1206
,共7页
曹杰%陈广银%常志州%叶小梅%杜静
曹傑%陳廣銀%常誌州%葉小梅%杜靜
조걸%진엄은%상지주%협소매%두정
猪场废水%秸秆床反应器%有机负荷%水力停留时间%沼气
豬場廢水%秸稈床反應器%有機負荷%水力停留時間%沼氣
저장폐수%갈간상반응기%유궤부하%수력정류시간%소기
piggery wastewater%straw-bed bioreactor%OLR%HRT%biogas
在实验室条件下,以打捆麦秸为固定相,以猪场废水为流动相,采用半连续进料方式,考察了不同猪场废水容积负荷对秸秆床反应器产沼气的影响.结果表明:发酵前25d,较高的猪场废水有机负荷对反应器产气有一定抑制,之后日产气量和容积产气量迅速增加,并明显高于低猪场废水有机负荷的处理,当猪场废水容积负荷为7.2kgCOD/(m3?d)时,厌氧反应器最大容积产气量达2.29m3/(m3?d),产气稳定后维持在1.52~1.76m3/(m3?d),较猪场废水容积负荷为2.4,1.44kgCOD/(m3?d)的处理分别提高了50%和130%以上,对产气中甲烷含量无明显影响;较高的猪场废水容积负荷不利于麦秸厌氧发酵产沼气,发酵后麦秸干物质损失率、纤维素和半纤维素分解率均与猪场废水容积负荷成反比,红外的结果与之一致.对发酵后麦秸水浸提液的DGGE检测表明,维持反应器高有机负荷、低发酵液HRT,促进了厌氧微生物在麦秸表面定植,微生物种群数量和丰富度均明显高于低有机负荷、高发酵液HRT的处理,反应器耐高有机负荷冲击的能力增强.采用秸秆床反应器处理农村常见的秸秆和畜禽养殖污水产沼气是可行的,且较高的废水有机负荷有利于提高反应器容积产气率.
在實驗室條件下,以打捆麥秸為固定相,以豬場廢水為流動相,採用半連續進料方式,攷察瞭不同豬場廢水容積負荷對秸稈床反應器產沼氣的影響.結果錶明:髮酵前25d,較高的豬場廢水有機負荷對反應器產氣有一定抑製,之後日產氣量和容積產氣量迅速增加,併明顯高于低豬場廢水有機負荷的處理,噹豬場廢水容積負荷為7.2kgCOD/(m3?d)時,厭氧反應器最大容積產氣量達2.29m3/(m3?d),產氣穩定後維持在1.52~1.76m3/(m3?d),較豬場廢水容積負荷為2.4,1.44kgCOD/(m3?d)的處理分彆提高瞭50%和130%以上,對產氣中甲烷含量無明顯影響;較高的豬場廢水容積負荷不利于麥秸厭氧髮酵產沼氣,髮酵後麥秸榦物質損失率、纖維素和半纖維素分解率均與豬場廢水容積負荷成反比,紅外的結果與之一緻.對髮酵後麥秸水浸提液的DGGE檢測錶明,維持反應器高有機負荷、低髮酵液HRT,促進瞭厭氧微生物在麥秸錶麵定植,微生物種群數量和豐富度均明顯高于低有機負荷、高髮酵液HRT的處理,反應器耐高有機負荷遲擊的能力增彊.採用秸稈床反應器處理農村常見的秸稈和畜禽養殖汙水產沼氣是可行的,且較高的廢水有機負荷有利于提高反應器容積產氣率.
재실험실조건하,이타곤맥갈위고정상,이저장폐수위류동상,채용반련속진료방식,고찰료불동저장폐수용적부하대갈간상반응기산소기적영향.결과표명:발효전25d,교고적저장폐수유궤부하대반응기산기유일정억제,지후일산기량화용적산기량신속증가,병명현고우저저장폐수유궤부하적처리,당저장폐수용적부하위7.2kgCOD/(m3?d)시,염양반응기최대용적산기량체2.29m3/(m3?d),산기은정후유지재1.52~1.76m3/(m3?d),교저장폐수용적부하위2.4,1.44kgCOD/(m3?d)적처리분별제고료50%화130%이상,대산기중갑완함량무명현영향;교고적저장폐수용적부하불리우맥갈염양발효산소기,발효후맥갈간물질손실솔、섬유소화반섬유소분해솔균여저장폐수용적부하성반비,홍외적결과여지일치.대발효후맥갈수침제액적DGGE검측표명,유지반응기고유궤부하、저발효액HRT,촉진료염양미생물재맥갈표면정식,미생물충군수량화봉부도균명현고우저유궤부하、고발효액HRT적처리,반응기내고유궤부하충격적능력증강.채용갈간상반응기처리농촌상견적갈간화축금양식오수산소기시가행적,차교고적폐수유궤부하유리우제고반응기용적산기솔.
Influence of organic loading rate (OLR) of piggery wastewater on biogas production of straw-bed bioreactor was conducted under (37±1)℃at lab scale. Higher OLR of piggery wastewater was adverse to biogas production during day 0to 25, and then daily biogas yield and volume biogas yield increased rapidly and higher than that of treatment with lower organic loading rate of piggery wastewater. The highest volume biogas yield of 2.29m3/(m3·d) was obtained at 34d with OLR of piggery wastewater of 7.2kgCOD/(m3·d). Volume biogas yield of treatment with OLR of piggery wastewater of 7.2kgCOD/(m3·d) was 1.52~1.76m3/(m3·d) which was 50% and 130% higher than that of treatment with OLR of piggery wastewater of 2.4and 1.44kgCOD/(m3·d). The higher OLR of piggery wastewater was adverse to biogas production of wheat straw and higher OLR of piggery wastewater with lower total solid, cellulose and hemicelloluse removal rate which was consistent with the result of FTIR. The result of DGGE of water extract of digested wheat straw showed that higher OLR of piggery wastewater promoted the colonization of microorganisms in the straw surface and anaerobic microbial community structure and number were much more than that of treatment with lower organic loading rate of piggery wastewater. It was feasible to use straw-bed bioreactor for biogas production with agricultural straw and livestock wastewater as fermentation materials and higher OLR of livestock wastewater with higher volume biogas yield.