化学反应工程与工艺
化學反應工程與工藝
화학반응공정여공예
CHEMICAL REACTION ENGINEERING AND TECHNOLOGY
2001年
2期
153-158
,共6页
郑成%黄开勋%郑广畴%黄格昕%方伟光
鄭成%黃開勛%鄭廣疇%黃格昕%方偉光
정성%황개훈%정엄주%황격흔%방위광
纸浆蔗渣%酶法水解%酶反应器%酶吸附,%酶活性
紙漿蔗渣%酶法水解%酶反應器%酶吸附,%酶活性
지장자사%매법수해%매반응기%매흡부,%매활성
以蒸煮时间5.5小时,温度为155~160℃,P=0.6MPa, pH为4.5的40目的纸浆蔗渣为底物,日本Yakult生物化学试剂公司的Onozuka-R-10纤维素酶为催化剂,在50℃,pH为4.8(乙酸—乙酸钠缓冲液)的条件下,考察了釜式和固定床反应器对酶解反应过程的影响,测定了在不同底物浓度时的酶解反应还原糖得率、探讨了酶的吸附以及酶活性在酶解反应过程的变化情况。实验结果表明:在本实验条件下,底物浓度高,转化率则低;固定床反应器对酶的吸附比釜式反应器略多;酶的活性变化在两种反应器型式中几乎没多大差别。
以蒸煮時間5.5小時,溫度為155~160℃,P=0.6MPa, pH為4.5的40目的紙漿蔗渣為底物,日本Yakult生物化學試劑公司的Onozuka-R-10纖維素酶為催化劑,在50℃,pH為4.8(乙痠—乙痠鈉緩遲液)的條件下,攷察瞭釜式和固定床反應器對酶解反應過程的影響,測定瞭在不同底物濃度時的酶解反應還原糖得率、探討瞭酶的吸附以及酶活性在酶解反應過程的變化情況。實驗結果錶明:在本實驗條件下,底物濃度高,轉化率則低;固定床反應器對酶的吸附比釜式反應器略多;酶的活性變化在兩種反應器型式中幾乎沒多大差彆。
이증자시간5.5소시,온도위155~160℃,P=0.6MPa, pH위4.5적40목적지장자사위저물,일본Yakult생물화학시제공사적Onozuka-R-10섬유소매위최화제,재50℃,pH위4.8(을산—을산납완충액)적조건하,고찰료부식화고정상반응기대매해반응과정적영향,측정료재불동저물농도시적매해반응환원당득솔、탐토료매적흡부이급매활성재매해반응과정적변화정황。실험결과표명:재본실험조건하,저물농도고,전화솔칙저;고정상반응기대매적흡부비부식반응기략다;매적활성변화재량충반응기형식중궤호몰다대차별。
Paper pulp bagasse celluloses were pretreated under the conditions of τ=5.5h, T=155-160℃,P=0.6MPa,pH=4.5. The size of paper pulp bagasse celluloses was 40 meshes. The Yakult 0nozuka R-10 cellulase was used in the experiments. The paper pulp bagasse cellulose enzymatic hydrolysis were carried out in a tank reactor and/or a fixed bed reactor under the conditions of T=50℃, pH=4.8. The hydrolysis reducing sugar yields, enzyme adsorptivity and activity were inspected for different cellulose concentrations. The experiment results indicated that the higher bagasse concentration, the lower reducing sugar yields,and the enzyme adsorption amount were more in the fixed bed reactor than in the tank reactor in the experimental conditions. The enzyme activity changes with hydrolysis were closed in the two type reactors. The enzyme activity decrease was relatively quick in the first 20hr. It was experimentally observed that enzyme always loses its entire activity when the reaction periods exceed 140hr (close 6 days).