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Hydrodeoxygenation of feedstock derived from renewable sources with limited decarboxylation conversion using nickel and molybdenum based catalysts

机译:使用镍和钼基催化剂对脱羧转化率受限的可再生资源原料进行加氢脱氧

摘要

Hydrodeoxygenation of charges obtained from renewable sources with 10% conversion by decarboxylation/decarbonylation, by implementing a mass catalyst or support comprising an active phase constituted of at least one element of group VIB and at least one group VIII element, where the elements are as sulfide and the atomic ratio of metal of group VIII to metal of the group VIB is strictly greater than 0 to less than 0.095, the process is carried out e.g. at a temperature of 120-450[deg] C, and at a pressure of 1-10 MPa, is claimed. Process for hydrodeoxygenation of charges obtained from renewable sources with 10% conversion by decarboxylation/decarbonylation, implementing a mass catalyst or support comprising an active phase constituted of at least one element of group VIB and at least one group VIII element, where the elements are as sulfide and the atomic ratio of metal (or metals) of group VIII to metal (or metals) of the group VIB is strictly greater than 0 to less than 0.095, the process is carried out at a temperature of 120-450[deg] C, at a pressure of 1-10 MPa, at a space velocity of 0.1-10 h - 1and in the presence of a total amount of hydrogen mixed with charge such as the ratio of hydrogen/charge is 50-3000 Nm 3of hydrogen/m 3of charge, is claimed.
机译:通过实施包含由至少一种VIB族元素和至少一种VIII族元素组成的活性相的块状催化剂或载体,通过脱羧/脱羰基反应从可再生资源中获得的电荷进行加氢脱氧,转化率为10%并且第VIII族金属与第VIB族金属的原子比严格地大于0至小于0.095,该方法例如进行要求保护的温度为120-450℃,压力为1-10MPa。通过脱羧/脱羰基使可再生资源中的电荷加氢脱氧的方法,其转化率为10%,实现了包含活性相的块状催化剂或载体,该活性相由至少一种VIB族元素和至少一种VIII族元素组成,其中元素为硫化物且VIII族金属(一种或多种金属)与VIB族金属(一种或多种金属)的原子比严格大于0至小于0.095,该方法在120-450℃的温度下进行,在1-10 MPa的压力下,在0.1-10 h-> 1>的空速下,并且在存在与电荷混合的总量为氢(例如氢/电荷之比)的情况下为50-3000 Nm 3要求>氢气/ m 3电荷。

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