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    • 61. 发明授权
    • Process for producing acrolein and acrylic acid
    • 制备丙烯醛和丙烯酸的方法
    • US08404889B2
    • 2013-03-26
    • US12662123
    • 2010-03-31
    • Michio TanimotoHideo Onodera
    • Michio TanimotoHideo Onodera
    • C07C51/16C07C45/00
    • C07C45/35C07C51/252C07C47/22C07C57/04
    • The invention offers an improvement in a process for start-up in the occasion of producing acrolein and acrylic acid by catalytically oxidizing propylene at vapor phase under high load conditions, the start-up meaning the step of increasing the propylene supply rate (loading) from the non-reacting condition to the prescribed reaction conditions. This process is characterized in that the propylene supply rate is increased in the start-up stage of the reaction until the prescribed composition of starting reactant gas and the flow rate of the starting reactant gas are obtained, while adjusting at least one of the reaction temperature, the composition of the starting reactant gas and flow rate of the starting reactant gas, so as to maintain the propylene conversion at not lower than 90 mol %, the maximum peak temperature of the catalyst layer in each reaction zone at no higher than 450° C., and the sum of each ΔT (maximum peak temperature of a catalyst layer—reaction temperature) at the catalyst layer in each of the reaction zones to be no more than 180° C., respectively. According to this process, the reaction speedily reaches the steady state (standard operating conditions) and a high acrolein and acrylic acid yield is stably achieved from the start of the reaction.
    • 本发明提供了在高负载条件下通过在气相下催化氧化丙烯来生产丙烯醛和丙烯酸的情况下的启动方法的改进,启动意味着将丙烯供应速率(负载)从 对规定的反应条件的非反应条件。 该方法的特征在于,在反应的启动阶段,丙烯供给速率增加,直到获得规定的起始反应气体组成和起始反应气体的流量,同时调节至少一个反应温度 ,起始反应物气体的组成和起始反应气体的流速,以保持丙烯转化率不低于90mol%,各反应区中催化剂层的最高峰值温度不高于450° C,以及每个反应区域中的催化剂层的每个&Dgr; T(催化剂层 - 反应温度的最大峰值温度)的总和分别不超过180℃。 根据该方法,反应快速达到稳定状态(标准操作条件),从反应开始就可以稳定地获得高丙烯醛和丙烯酸的收率。
    • 62. 发明授权
    • Process for producing acrylic acid
    • 丙烯酸生产工艺
    • US08318978B2
    • 2012-11-27
    • US12659994
    • 2010-03-26
    • Michio TanimotoHideo Onodera
    • Michio TanimotoHideo Onodera
    • C07C51/16C07C45/52
    • C07C51/252C07C57/04
    • The invention offers an improvement in a process for start-up in the occasion of producing acrylic acid by catalytically oxidizing acrolein at vapor phase under high load conditions, the start-up meaning the step of increasing the acrolein supply rate (loading) from the non-reacting condition to the prescribed reaction conditions. This process is characterized in that the acrolein supply rate is increased in the start-up stage of the reaction until the prescribed composition of starting reactant gas and the flow rate of the starting reactant gas are obtained, while adjusting at least one of the reaction temperature, the composition of the starting reactant gas and the flow rate of the starting reactant gas, so as to maintain the acrolein conversion at not lower than 90 mol %, the maximum peak temperature of the catalyst layer in each reaction zone at no higher than 400° C., and the sum of each ΔT (maximum peak temperature of a catalyst layer-reaction temperature) at the catalyst layer in each of the reaction zones to be no more than 150° C., respectively. According to this process, the reaction speedily reaches the steady state (standard operating conditions) and a high acrylic acid yield is stably achieved from the start of the reaction.
    • 本发明提供了在高负载条件下通过在气相下催化氧化丙烯醛来生产丙烯酸的情况下的启动方法的改进,启动意味着提高丙烯醛供应速率(负载) 反应条件达到规定的反应条件。 该方法的特征在于,在反应开始阶段丙烯醛供应速率增加,直到获得规定的起始反应气体组成和起始反应气体的流量,同时调节至少一个反应温度 ,起始反应气体的组成和起始反应气体的流量,以使丙烯醛的转化率保持在不低于90mol%,催化剂层在每个反应区中的最大峰值温度不高于400℃ ℃,以及每个反应区域中的催化剂层的每个&Dgr; T(催化剂层 - 反应温度的最大峰值温度)的总和分别不超过150℃。 根据该方法,反应快速达到稳定状态(标准操作条件),从反应开始就稳定地得到高丙烯酸收率。
    • 65. 发明授权
    • Catalyst and process for production of acrylic acid
    • 用于生产丙烯酸的催化剂和方法
    • US07030269B2
    • 2006-04-18
    • US10684285
    • 2003-10-13
    • Hiromi YunokiMichio Tanimoto
    • Hiromi YunokiMichio Tanimoto
    • C07C51/232
    • C07C51/252B01J21/12B01J23/002B01J23/8877B01J37/0018B01J37/0223B01J2523/00C07C57/04B01J2523/17B01J2523/55B01J2523/68B01J2523/69
    • There are disclosed: a catalyst which can be used for production of acrylic acid and is excellent in the catalytic performances (e.g. conversion of starting material, selectivity of aimed product) and further has very high physical strength; and a process for production of acrylic acid using this catalyst. The above catalyst for production of acrylic acid is a catalyst which is obtained by a process including the steps of: heating a mixed liquid of starting materials including molybdenum and vanadium as essential components; and then molding the resultant dried material with a liquid binder; and then calcining the resultant molding; with the catalyst being characterized in that the liquid binder is an aqueous liquid of 7.0 to 10.0 in pH. The above process for production of acrylic acid is a process which comprises the step of carrying out catalytic gas phase oxidation of acrolein in the presence of molecular oxygen, thereby producing the acrylic acid; with the process being characterized by using the above catalyst for production of acrylic acid according to the present invention.
    • 公开了可用于生产丙烯酸的催化剂,催化性能(例如起始原料的转化,目标产物的选择性)优异,并且还具有非常高的物理强度; 以及使用该催化剂生产丙烯酸的方法。 上述用于制备丙烯酸的催化剂是通过包括以下步骤的方法获得的催化剂:将包含钼和钒的原料的混合液作为必要成分加热; 然后用液体粘合剂将得到的干燥材料成型; 然后煅烧所得成型品; 催化剂的特征在于液体粘合剂是pH为7.0至10.0的水性液体。 上述丙烯酸的制造方法是在分子氧的存在下进行丙烯醛的催化气相氧化的工序,由此生成丙烯酸; 该方法的特征在于使用上述催化剂制备本发明的丙烯酸。