农业工程学报
農業工程學報
농업공정학보
2013年
17期
182-187
,共6页
杨世关%肖婷%李继红%董长青
楊世關%肖婷%李繼紅%董長青
양세관%초정%리계홍%동장청
秸秆%沼气%发酵%成型燃料
秸稈%沼氣%髮酵%成型燃料
갈간%소기%발효%성형연료
straw%biogas%fermentation%densified biomass fuel
针对秸秆压缩成型存在设备磨损严重和厌氧发酵面临的抗生物降解屏障,提出了一种秸秆厌氧发酵改性制备成型燃料的思路并进行了试验研究。以玉米秸秆为原料,在总固体质量分数12%和中温38℃下对原料分别进行为期10和20 d的厌氧发酵,发酵后的沼渣经粉碎和干燥后于100℃、6 MPa条件下压缩成直径10 mm的颗粒燃料。试验结果表明:经过10和20 d的发酵,玉米秸秆所含能量仅有14.49%和32.01%转移到沼气中;沼渣弹筒发热量分别达到18.01和18.05 MJ/kg,高于原料的17.02 MJ/kg;沼渣挥发物质质量分数为74.08%和72.63%,比原料的81.02%分别下降了8.6%和10.4%;沼渣木质素质量分数为16.98%和17.92%,比原料的13.65%分别增加了24.4%和31.3%;沼渣苯醇抽提物质量分数为5.66%和4.86%,比原料的7.52%分别降低了24.7%和35.4%。成型试验结果表明:沼渣制成的成型燃料松弛密度分别为1.041 g/cm3和1.150 g/cm3,比未发酵秸秆的1.019 g/cm3分别提高了2.2%和12.86%。厌氧发酵改性有助于提高秸秆成型性能、制粒达到相同松弛密度所需的压力较小,有助于降低成型过程设备磨损,且基于上述思路形成的气固二元燃料生产工艺,使秸秆的转化利用不再受制于抗降解屏障,值得深入研究。
針對秸稈壓縮成型存在設備磨損嚴重和厭氧髮酵麵臨的抗生物降解屏障,提齣瞭一種秸稈厭氧髮酵改性製備成型燃料的思路併進行瞭試驗研究。以玉米秸稈為原料,在總固體質量分數12%和中溫38℃下對原料分彆進行為期10和20 d的厭氧髮酵,髮酵後的沼渣經粉碎和榦燥後于100℃、6 MPa條件下壓縮成直徑10 mm的顆粒燃料。試驗結果錶明:經過10和20 d的髮酵,玉米秸稈所含能量僅有14.49%和32.01%轉移到沼氣中;沼渣彈筒髮熱量分彆達到18.01和18.05 MJ/kg,高于原料的17.02 MJ/kg;沼渣揮髮物質質量分數為74.08%和72.63%,比原料的81.02%分彆下降瞭8.6%和10.4%;沼渣木質素質量分數為16.98%和17.92%,比原料的13.65%分彆增加瞭24.4%和31.3%;沼渣苯醇抽提物質量分數為5.66%和4.86%,比原料的7.52%分彆降低瞭24.7%和35.4%。成型試驗結果錶明:沼渣製成的成型燃料鬆弛密度分彆為1.041 g/cm3和1.150 g/cm3,比未髮酵秸稈的1.019 g/cm3分彆提高瞭2.2%和12.86%。厭氧髮酵改性有助于提高秸稈成型性能、製粒達到相同鬆弛密度所需的壓力較小,有助于降低成型過程設備磨損,且基于上述思路形成的氣固二元燃料生產工藝,使秸稈的轉化利用不再受製于抗降解屏障,值得深入研究。
침대갈간압축성형존재설비마손엄중화염양발효면림적항생물강해병장,제출료일충갈간염양발효개성제비성형연료적사로병진행료시험연구。이옥미갈간위원료,재총고체질량분수12%화중온38℃하대원료분별진행위기10화20 d적염양발효,발효후적소사경분쇄화간조후우100℃、6 MPa조건하압축성직경10 mm적과립연료。시험결과표명:경과10화20 d적발효,옥미갈간소함능량부유14.49%화32.01%전이도소기중;소사탄통발열량분별체도18.01화18.05 MJ/kg,고우원료적17.02 MJ/kg;소사휘발물질질량분수위74.08%화72.63%,비원료적81.02%분별하강료8.6%화10.4%;소사목질소질량분수위16.98%화17.92%,비원료적13.65%분별증가료24.4%화31.3%;소사분순추제물질량분수위5.66%화4.86%,비원료적7.52%분별강저료24.7%화35.4%。성형시험결과표명:소사제성적성형연료송이밀도분별위1.041 g/cm3화1.150 g/cm3,비미발효갈간적1.019 g/cm3분별제고료2.2%화12.86%。염양발효개성유조우제고갈간성형성능、제립체도상동송이밀도소수적압력교소,유조우강저성형과정설비마손,차기우상술사로형성적기고이원연료생산공예,사갈간적전화이용불재수제우항강해병장,치득심입연구。
Corn straw is one of the major crop straws considered for producing renewable fuels and energy in China. Production of densified biomass fuel (DBF) and biogas from corn straw are two main conversion approaches. One of the major problems associated with the DBF production from corn straw is rapid wear of the briquetting/pelleting unit. The primary technical barrier for anaerobic fermentation of corn straw is its recalcitrance structure. Aiming at these problems, we proposed a process of DBF production from corn straw pretreated by anaerobic fermentation. In this process, corn straw is firstly anaerobicly digested to produce biogas, and then the solid digestate is pressed into DBF. In order to prove the feasibility of this process, the anaerobic fermentation experiments were performed at 38℃at 12%of total solid (TS). The experiments were divided into two groups with a digestion period of 10 and 20 days, respectively. After anaerobic digestion, the digestate was shed, dried, and pressed into DBF with a diameter of 10mm in a hydraulic device at pressure up to 6 MPa and a temperature of 100℃. The anaerobic experimental results showed that after 10 and 20 days of anaerobic fermentation, 14.49%and 32.01%of the energy contained by corn straw was converted to biogas energy, and the characteristics of digestate were beneficial to DBF production in terms of lignin and extract contents. The lignin content of solid digestate was elevated to 16.98%and 17.92%, and increased by 24.4%and 31.3%compared to 13.65%of corn straw. <br> The benzene alcohol extract of solid digestate was lowered to 5.66% and 4.86%, and decreased by 24.7%and 35.4%compared to 7.52%of corn straw. At the same time, the characteristic changes of solid digestate on aspects of heat value and volatile content were in favor of improving DBF quality:the bomb calorific values of solid digestate reached 18.01 and 18.05 MJ/kg, higher than the 17.02 MJ/kg of raw material, and the volatile contents of solid digestate reached 74.08%and 72.63%, decreased by 8.6%and 10.4%than the 81.02%of raw material. The DBF production results illustrated that the relaxation densities were 1.041 and 1.150 g/cm3, respectively for DBFs produced with solid digestate obtained from anaerobic fermentation for 10 and 20 days, and increased by 2.2% and 12.86% compared to1.019 g/cm3 of DBF produced with corn straw. In conclusion, co-production of DBF and biogas from corn straw based on anaerobic fermentation has the potential of helping to reduce the wear of a briquetting/pelleting unit in its densification process, and avoiding a recalcitrance structure obstacle in its anaerobic fermentation.