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Aqueous phase hydrodechlorination of 2,4-dichlorophenol over supported palladium catalysts.

机译:负载型钯催化剂上的2,4-二氯苯酚水相加氢脱氯。

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The feasibility of aqueous phase chlorophenol hydrodechlorination (HDC) reaction at 273-303 K has been demonstrated for commercial available Pd/C, Pd/Al2O3 and Rh/C catalysts. The relative importance of the transport/kinetic processes were considered in the case of 2,4-dichlorophenol (DCP) HDC over Pd/C and Pd/Al2O3 catalysts. In 2,4-DCP HDC over a 1% w/w Pd/C and 1% w/w Pd/Al2O 3 at 303 K, operated in the kinetic controlled regime, 2-chlorophenol is the only intermediate partially dechlorinated product which reacts further to yield phenol; cyclohexanone is formed over Pd/Al2O3 prior to the completion of dechlorination. Reuse of the catalysts revealed an appreciable deactivation of Pd/C and a limited loss of activity in the case of Pd/Al2O3 Deactivation of Pd/C can be linked to a decrease (up to ca. 60%) in the initial BET surface area allied to appreciable leaching (up to ca. 40%) of the starting Pd content through the corrosive action of HCl that is generated during HDC. Inclusion of HCl in the reaction mixture (pH = 5-1.5) resulted in a marked decline in the initial HDC rate associated with Pd/Al2O 3 and a lesser drop in HDC activity for Pd/C. 2,4-DCP HDC with/without the addition of NaOH, NH4OH, LiOH, KOH, RbOH and CsOH (solution pH = 13-1.5) revealed an increase in fractional dechlorination with the addition of base, which can be attributed to a suppression of HCl inhibition. The initial HDC activity and selectivity delivered by both catalysts were pH dependent and differences in response to bulk solution pH variations are discussed in terms of the nature of the reactive species in solution and the amphoteric behavior of the Pd supports. Starting in the range 7-11.6, solution pH during 2,4-DCP HDC over Pd/Al2O3 can be controlled to within +/-0.13 with a continuous supply of NaOH solution. HDC operating under controlled pH exhibited a maximum activity in the pH range 7-8. The initial conversion of 2,4-DCP to 2-CP follows an Langmuir-Hinshelwood kinetic mechanism with rate inhibition at high 2,4-DCP concentrations (>20 mmol dm-3 ). The pH effect on initial HDC activity was analyzed by a generic correlation.
机译:对于市售的Pd / C,Pd / Al2O3和Rh / C催化剂,已经证明了在273-303 K下进行水相氯酚加氢脱氯(HDC)反应的可行性。在Pd / C和Pd / Al2O3催化剂上使用2,4-二氯苯酚(DCP)HDC时,考虑了运输/动力学过程的相对重要性。在303 K下以1%w / w Pd / C和1%w / w Pd / Al2O 3进行的2,4-DCP HDC中,以动力学控制方式进行操作时,2-氯苯酚是唯一发生反应的中间体部分脱氯产物进一步产生苯酚;脱氯完成前,在Pd / Al2O3上形成环己酮。催化剂的重复使用表明Pd / C明显失活,而在Pd / Al2O3情况下活性有限损失Pd / C失活可能与初始BET表面积的减少(最多约60%)有关。通过在HDC期间产生的HCl的腐蚀作用,可明显地浸出(最多约40%)起始Pd含量。反应混合物中加入HCl(pH = 5-1.5)导致与Pd / Al2O 3相关的初始HDC速率显着下降,而HDC活性对Pd / C的下降较小。添加或不添加NaOH,NH4OH,LiOH,KOH,RbOH和CsOH(溶液pH = 13-1.5)的2,4-DCP HDC显示,添加碱可提高部分脱氯率,这可归因于抑制作用抑制HCl。两种催化剂提供的初始HDC活性和选择性均取决于pH,并根据溶液中反应性物种的性质和Pd载体的两性行为讨论了对整体溶液pH变化的响应差异。从7-11.6开始,在连续提供NaOH溶液的情况下,可以将Pd / Al2O3上2,4-DCP HDC期间的溶液pH控制在+/- 0.13之内。在受控pH下操作的HDC在7-8的pH范围内表现出最大的活性。 2,4-DCP初始转化为2-CP遵循Langmuir-Hinshelwood动力学机理,在高2,4-DCP浓度(> 20 mmol dm-3)时速率受到抑制。通过通用相关性分析了pH对HDC初始活性的影响。

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