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Clean synthesis of adipic acid from cyclohexene in microemulsions with stearyl dimethyl benzyl ammonium chloride as surfactant: From the laboratory to bench scale

机译:以硬脂基二甲基苄基氯化铵为表面活性剂,在微乳液中由环己烯清洁合成己二酸:从实验室到实验室规模

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摘要

Adipic acid, HOOC(CH2)4COOH, is a white crystalline solid used primarily in the manufacture of nylon-6,6 polyamide. In industry, adipic acid is mainly produced by oxidation of cyclohexane with air and nitric acidfollowing a homogeneous two-step route. However, this process leads to the formation of nitrous oxide, a greenhouse gas that has to be decomposed. The aim of this study was the development of a clean technology at pilot scale in order to obtain and recover pure adipic acid, and the evaluation of its industrial practicability. Adipic acid was synthesized from cyclohexene and hydrogen peroxide in microemulsions with stearyl dimethyl benzyl ammonium chloride as surfactant. The non-polluting catalyst sodium tungstate, which contains no heavy metal, was used and the reaction conducted under mild conditions (85 C, 8 h). Yields of up to 81% were reached at the 0.14 L scale. However at the end of the reaction the catalyst and the surfactant must be separated and recycled for subsequent cycles. The reuse of the reaction media enabled the conversion to be increased up to 92% but a loss of surfactant and/or catalyst through the cycles progressively reduced the yields. Yields at the bench scale (1.4 L) increased during the two first cycles and then decreased to conversions of between 60% and 70%. Globally the yield is a little lower at bench scale. The results obtained show that the synthesis of adipic acid by a heterogeneous one-step oxidation of cyclohexene in the presence of hydrogen peroxide is an attractive route for developing a future green industrial process.
机译:己二酸HOOC(CH2)4COOH是一种白色结晶固体,主要用于尼龙6,6聚酰胺的生产。在工业上,己二酸主要是通过按照均匀的两步路线,用空气和硝酸氧化环己烷来生产的。但是,此过程导致形成一氧化二氮,这是一种必须分解的温室气体。这项研究的目的是开发一种中试规模的清洁技术,以便获得和回收纯己二酸,并对其工业实用性进行评估。以硬脂基二甲基苄基氯化铵为表面活性剂,由环己烯和过氧化氢在微乳液中合成己二酸。使用不含重金属的无污染的钨酸钠催化剂,反应在温和的条件下(85℃,8小时)进行。在0.14 L规模下,收率高达81%。然而,在反应结束时,必须将催化剂和表面活性剂分离并再循环用于随后的循环。反应介质的重复使用使转化率提高到92%,但是通过循环的表面活性剂和/或催化剂的损失逐渐降低了收率。在前两个周期中,基准规模的产量(1.4升)有所增加,然后下降到60%至70%之间。在全球范围内,单产规模的产量略低。获得的结果表明,在过氧化氢的存在下,通过环己烯的异相一步氧化来合成己二酸是开发未来绿色工业方法的有吸引力的途径。

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