1-丁烯氧化脱氢制丁二烯反应过程研究

Study on reaction process for oxidative dehydrogenation of 1-butene to butadiene

在320~560℃,0.06MPa^0.1MPa(g),氧烯比和水烯比(物质的量比)分别为0.55~0.85、11~20的条件下,使用自制丁烯氧化脱氢HS-2型催化剂在等温积分反应器中,研究了1-丁烯生成丁二烯的反应过程,并考察了原料丁烯组成及操作条件对丁烯转化率、丁二烯选择性的影响。实验结果表明:随着温度的升高,1-丁烯转化率先增加后基本保持不变,丁二烯的选择性基本不变;随着氧烯比的升高,1-丁烯转化率渐渐增大,丁二烯选择性随着氧烯比的升高,下降不明显;水烯比对丁二烯选择性影响不大,水烯比升高使得1-丁烯转化率略有降低;铁系催化剂HS-2的活性温度区间较宽,可适用于绝热反应器;丁烯原料可选1-丁烯和2-丁烯(顺、反丁烯)混合物。

The reaction process of 1-butene oxidative dehydrogenation to butadiene over catalyst HS-2 in an isothermal integral fixed bed reactor was studied, and the effects of feedstock composition and reaction conditions on the conversion of 1-butene and selectivity of butadiene were investigated.The results indicated that the conversion of 1-butene first increased then remained nearly constant and the selectivity of butadiene almost kept unchanged with increasing temperature; the conversion of 1-butene gradually increased and the selectivity of butadiene declined insignificantly with increasing mole ratio of oxygen to 1-butene; the conversion of 1-butene decreased slightly with increasing mole ratio of water to 1-butene which had little effect on the selectivity of butadiene; iron-based catalyst HS-2 could be used in a wide temperature scope, so it would be suitable for the adiabatic reactor; and the mixed butenes containing 1-butene and 2-butene could be selected as reactant.