Как выбрать гостиницу для кошек
14 декабря, 2021
Lower temperature operation with reduced sugar degradation is achieved by adding a small amount of mineral acid to the pretreatment process. The acid increases reaction rates at a given temperature and the ratio of hydrolysis rate to the degradation rate is also increased.
A compromise between the reaction temperature and the reaction time exists for acid-catalyzed reactions. As for autohydrolysis, however, conditions explored range from several hours at 100°C to 10 seconds at 200°C with a sulfuric acid concentration of 0.5 to 4.0%. Acid catalysts have also been used in steam explosion systems with similar results. Xylose yields generally range from 70 to 95%. However, sulfuric acid processes produce lignin that is more condensed (52% of the lignin extractable in dilute NaOH) than that produced by an autohydrolysis system. Sulfur dioxide has also been investigated as a catalyst to improve the efficiency of the pretreatments. Use of excess water increases energy consumption and decreases the concentration of xylose in the hydrolyzate, thus decreasing the concentration of ethanol that can be produced in the xylose fermentation step. In a study by Ojumu and Ogunkunle [51], production of glucose was achieved in batch reactors from hydrolysis of lignocellulose under extremely low acid (ELA) concentration and high-temperature condition by pretreating the sawdust by autohydrolysis ab initio. The maximum glucose yield obtained was reported to be 70% for the pretreated sawdust at 210°C in the eighteenth minute of the experiment. This value is about 1.4 times the maximum glucose level obtained from the untreated sawdust under the nominally same condition [51].
The acid hydrolysis process has a long history of over 100 years. As an alternative to dilute acid hydrolysis, concentrated acid-based hydrolysis processes are also conceivable and available. However, these types of processes are generally more expensive to operate and render handling difficulties [52]. Sulfuric acid is the most common choice of catalyst; however, other mineral acids such as hydrochloric, nitric, and trifluoroacetic acids (CF3COOH) have also been used.