农业工程学报
農業工程學報
농업공정학보
2014年
8期
174-180
,共7页
胡建军%周雪花%郭婕%荆艳艳%张全国
鬍建軍%週雪花%郭婕%荊豔豔%張全國
호건군%주설화%곽첩%형염염%장전국
秸秆%氢气%微生物%初始温度%光合细菌%反应热
秸稈%氫氣%微生物%初始溫度%光閤細菌%反應熱
갈간%경기%미생물%초시온도%광합세균%반응열
straw%hydrogen%microorganism%initial temperature%photosynthetic bacteria%reaction heat
秸秆微粉的光合细菌制氢过程是放热反应,引起的热效应会直接影响产氢效果。为了实现高效低能耗产氢,该文采用秸秆微化粉碎与酶水解预处理相结合的方法,利用自制的秸秆微粉光合细菌制氢反应热测试系统,进行了不同初始温度对秸秆微粉酶解光合细菌制氢反应热的影响试验研究,结果表明:当初始温度为30℃时,最大反应热约为7.1 kJ,最大产热速率约为1.01 kJ/h,反应末期累计反应热约为32.9 kJ,累计产氢量约为745.9 mL,光合细菌制氢反应最充分,产氢效果最好;累计产氢量和底物能量转化率可用累计反应热的二次多项式来表示,光能转化率可用累计反应热的三次多项式来表示。该研究结论可为揭示秸秆微粉酶解光合细菌制氢过程的热量释放变化规律,从生物反应热角度优化工艺参数和预测光合细菌制氢效果提供参考依据。
秸稈微粉的光閤細菌製氫過程是放熱反應,引起的熱效應會直接影響產氫效果。為瞭實現高效低能耗產氫,該文採用秸稈微化粉碎與酶水解預處理相結閤的方法,利用自製的秸稈微粉光閤細菌製氫反應熱測試繫統,進行瞭不同初始溫度對秸稈微粉酶解光閤細菌製氫反應熱的影響試驗研究,結果錶明:噹初始溫度為30℃時,最大反應熱約為7.1 kJ,最大產熱速率約為1.01 kJ/h,反應末期纍計反應熱約為32.9 kJ,纍計產氫量約為745.9 mL,光閤細菌製氫反應最充分,產氫效果最好;纍計產氫量和底物能量轉化率可用纍計反應熱的二次多項式來錶示,光能轉化率可用纍計反應熱的三次多項式來錶示。該研究結論可為揭示秸稈微粉酶解光閤細菌製氫過程的熱量釋放變化規律,從生物反應熱角度優化工藝參數和預測光閤細菌製氫效果提供參攷依據。
갈간미분적광합세균제경과정시방열반응,인기적열효응회직접영향산경효과。위료실현고효저능모산경,해문채용갈간미화분쇄여매수해예처리상결합적방법,이용자제적갈간미분광합세균제경반응열측시계통,진행료불동초시온도대갈간미분매해광합세균제경반응열적영향시험연구,결과표명:당초시온도위30℃시,최대반응열약위7.1 kJ,최대산열속솔약위1.01 kJ/h,반응말기루계반응열약위32.9 kJ,루계산경량약위745.9 mL,광합세균제경반응최충분,산경효과최호;루계산경량화저물능량전화솔가용루계반응열적이차다항식래표시,광능전화솔가용루계반응열적삼차다항식래표시。해연구결론가위게시갈간미분매해광합세균제경과정적열량석방변화규률,종생물반응열각도우화공예삼수화예측광합세균제경효과제공삼고의거。
In photosynthetic-bacteria hydrogen production with enzyme-hydrolyzed fine straws, the growth and reproduction of photosynthetic bacteria will occur in an appropriate temperature range, and the resulting heat effect will have direct influence on hydrogen production due to exothermic processes in the hydrogen production reaction of photosynthetic bacteria with organic acid. Therefore, the research on effects of initial temperature on the reaction heat in the photosynthetic-bacteria hydrogen production with enzyme-hydrolyzed fine straws, is helpful to figure out the heat release rule in such photosynthetic-bacteria hydrogen production, and thus, to provide proper control to the initial temperature to meet the purpose of efficient hydrogen production. In this paper, with the combination method of micro-grinding and enzyme hydrolysis of straws, blank control tests for reaction liquid were performed with photosynthetic hydrogen-production flora of F1, F5, F7, F11, L6, S7 and S9 screened out after flora enrichment, separation, and cultivation, by using a self-developed testing system for reaction heat in the photosynthetic-bacteria hydrogen production with fine straws. The tests were made with the conditions of fine maize straws of 53-61 μm, substrate concentration of 30 mg/mL, initial pH value of 7.0, illumination intensity of 2 000 lx, inoculation and non-inoculation of 20% photosynthetic mixed bacteria flora which was on the logarithmic growth phase, and at the initial temperatures of 25, 30 and 35℃, identifying the relations between reaction heat and reaction time at the three initial temperatures, variation characteristics of the heat production rate, variation characteristics of the cumulative reaction heat, and the relations between the cumulative reaction heat and the cumulative hydrogen production, optical energy conversion rate and substrate energy conversion rate; optimizing process parameters in the photosynthetic-bacteria hydrogen production reaction; and presenting the relations model of the cumulative reaction heat and the cumulative hydrogen production, optical energy conversion rate and substrate conversion rate. Research results showed that, different initial temperatures had significant influence on the result of photosynthetic-bacteria hydrogen production with fine maize straws. In case of initial temperature of 30℃, maximum reaction heat of approximately 7.1 kJ, maximum heat production rate of approximately 1.01 kJ/h, cumulative reaction heat of approximately 32.9 kJ at the end of reaction, and cumulative hydrogen production of approximately 745.9 mL, the photosynthetic-bacteria hydrogen production reaction was conducted to its most extent and yielded the best result. Although initial temperatures were different, the variations of reaction heat and cumulative heat reaction were basically the same, this was to say, their maximum heat production rate occurred at the reaction time of 8 h and their minimum heat production rate occurred at the reaction time of 12 h; With the increase of the cumulative reaction heat, the cumulative hydrogen production and the substrate energy conversion rate would increase, which could be expressed with a quadratic polynomial; with the increase of the cumulative reaction heat, the optical energy conversion rate would increase and decrease, which could be expressed with a cubic polynomial. These research results provide reference basis to reveal the heat release rule in the photosynthetic-bacteria hydrogen production with enzyme-hydrolyzed fine straws, and to optimize process parameters and predict the photosynthetic-bacteria hydrogen production result from the perspective of biologic reaction heat.