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    • 1. 发明授权
    • Process for the synthesis of DMAPA
    • 合成DMAPA的方法
    • US07939027B2
    • 2011-05-10
    • US12683015
    • 2010-01-06
    • Martin ErnstSteffen OehlenschlägerFrank KuhnkeKarl-Heinz RoβRoland DeegJohann-Peter Melder
    • Martin ErnstSteffen OehlenschlägerFrank KuhnkeKarl-Heinz RoβRoland DeegJohann-Peter Melder
    • B01J10/00C07C209/00B01J35/02B01J19/00B01J8/00
    • C07C209/48B01J2219/00006C07C253/30C07C211/11C07C255/24
    • The present invention relates to a process for the industrial preparation of a diamine starting from a corresponding alkenyl nitrile comprising at least one C—C double bond, which comprises the steps (a) reaction of the alkenyl nitrile with a corresponding monoamine in a first reactor so that the monoamine adds exothermically onto the at least one double bond to form an aminoalkyl nitrile, with the monoamine and water being charged initially and the alkenyl nitrile being fed in; (b) evaporation of unreacted alkenyl nitrile and monoamine to increase the concentration of the aminoalkyl nitrile product in the bottoms of the first reactor; (c) transfer of the aminoalkyl nitrile bottom product from step (b) to a second reactor; (d) batchwise catalytic hydrogenation of the aminoalkyl nitrile transferred in step (c) to the diamine in the second reactor, with each batch being obtained by initially charging a catalyst suitable for the hydrogenation of nitriles to amines and also water, the desired diamine and a base, introducing hydrogen into the second reactor and feeding in the aminoalkyl nitrile transferred in step (c); and (e) isolation of the diamine and, if appropriate, repetition of the steps (a) to (e). The invention further relates to an apparatus for preparing these diamines and the use of the apparatuses. A preferred diamine is 3-dimethylaminopropylamine (DMAPA).
    • 本发明涉及从包含至少一个C-C双键的相应链烯基腈开始工业制备二胺的方法,其包括步骤(a)在第一反应器中烯基腈与相应的单胺反应 使得单胺在至少一个双键上放热添加以形成氨基烷基腈,最初加入单胺和水,并加入链烯基腈; (b)蒸发未反应的烯基腈和单胺以增加第一反应器底部氨基烷基腈产物的浓度; (c)将氨基烷基腈底部产物从步骤(b)转移至第二反应器; (d)将步骤(c)中转移的氨基烷基腈分批催化氢化为第二反应器中的二胺,每个批次通过首先将适合于将腈氢化成的催化剂加入到胺中而得到,并且还需要水,所需的二胺和 碱,将氢气引入第二反应器并进料步骤(c)中转移的氨基烷基腈; 和(e)分离二胺,如果合适,重复步骤(a)至(e)。 本发明还涉及一种用于制备这些二胺的装置和该装置的用途。 优选的二胺是3-二甲基氨基丙胺(DMAPA)。
    • 2. 发明授权
    • Process for the synthesis of DMAPA
    • 合成DMAPA的方法
    • US07723547B2
    • 2010-05-25
    • US12092684
    • 2006-10-31
    • Martin ErnstSteffen OehlenschlägerFrank KuhnkeKarl-Heinz RoβRonald DeegJohann-Peter Melder
    • Martin ErnstSteffen OehlenschlägerFrank KuhnkeKarl-Heinz RoβRonald DeegJohann-Peter Melder
    • C07C209/48
    • B01J8/20B01D3/14B01J2219/00006B01J2219/00029B01J2219/0004C07C209/48C07C211/11
    • The present invention relates to a process for the industrial preparation of a diamine starting from a corresponding alkenyl nitrile comprising at least one C—C double bond, which comprises the steps (a) reaction of the alkenyl nitrile with a corresponding monoamine in a first reactor so that the monoamine adds exothermically onto the at least one double bond to form an aminoalkyl nitrile, with the monoamine and water being charged initially and the alkenyl nitrile being fed in; (b) evaporation of unreacted alkenyl nitrile and monoamine to increase the concentration of the aminoalkyl nitrile product in the bottoms of the first reactor; (c) transfer of the aminoalkyl nitrile bottom product from step (b) to a second reactor; (d) batchwise catalytic hydrogenation of the aminoalkyl nitrile transferred in step (c) to the diamine in the second reactor, with each batch being obtained by initially charging a catalyst suitable for the hydrogenation of nitriles to amines and also water, the desired diamine and a base, introducing hydrogen into the second reactor and feeding in the aminoalkyl nitrile transferred in step (c); and (e) isolation of the diamine and, if appropriate, repetition of the steps (a) to (e). The invention further relates to an apparatus for preparing these diamines and the use of the apparatuses. A preferred diamine is 3-dimethylaminopropylamine (DMAPA).
    • 本发明涉及从包含至少一个C-C双键的相应链烯基腈开始工业制备二胺的方法,其包括步骤(a)在第一反应器中烯基腈与相应的单胺反应 使得单胺在至少一个双键上放热添加以形成氨基烷基腈,最初加入单胺和水,并加入链烯基腈; (b)蒸发未反应的烯基腈和单胺以增加第一反应器底部氨基烷基腈产物的浓度; (c)将氨基烷基腈底部产物从步骤(b)转移至第二反应器; (d)将步骤(c)中转移的氨基烷基腈分批催化氢化为第二反应器中的二胺,每个批次通过首先将适合于将腈氢化成的催化剂加入到胺中而得到,并且还需要水,所需的二胺和 碱,将氢气引入第二反应器并进料步骤(c)中转移的氨基烷基腈; 和(e)分离二胺,如果合适,重复步骤(a)至(e)。 本发明还涉及一种用于制备这些二胺的装置和该装置的用途。 优选的二胺是3-二甲基氨基丙胺(DMAPA)。
    • 5. 发明授权
    • Method for controlling the reactor admission temperature during the production of methylamine
    • 在甲胺生产过程中控制反应器入口温度的方法
    • US07518020B2
    • 2009-04-14
    • US10573185
    • 2004-09-24
    • Werner ReutemannRolf WambsganβFrank PoplowTheodor WeberKarl-Heinz RoβManfred Julius
    • Werner ReutemannRolf WambsganβFrank PoplowTheodor WeberKarl-Heinz RoβManfred Julius
    • C07C209/16
    • C07C209/16C07C211/04
    • The invention relates to a process for preparing methylamines by gas-phase reaction of methanol and ammonia as starting materials at a pressure in the range from 15 to 30 bar in the presence of heterogeneous catalyst. The starting materials are vaporized in one or more heat exchangers (1, 2, 3), superheated to produce a feed gas stream and subsequently fed into a reactor (4), with the mixing of the starting materials being able to be carried out in the feed stream to one of the heat exchangers (1, 2, 3) or at any desired position in a heat exchanger (1, 2, 3). A product gas stream comprising monomethylamine, dimethylamine and trimethylamine and also reaction by-products is taken off from the reactor (4). To control the reactor inlet temperature of the starting materials to a temperature in the range from 360° C. to 370° C., all or some of the feed gas stream or the product gas stream is passed through an adjustable valve (5) in order to vary the pressure and thus the condensation temperature.
    • 本发明涉及通过甲醇和氨作为起始原料在非均相催化剂存在下在15至30巴的压力下气相反应制备甲胺的方法。 起始材料在一个或多个热交换器(1,2,3)中蒸发,过热以产生进料气流,并随后进料到反应器(4)中,原料的混合能够进行 到一个热交换器(1,2,3)或在热交换器(1,2,3)中的任何期望位置的进料流。 从反应器(4)中取出包含一甲胺,二甲胺和三甲胺以及反应副产物的产物气流。 为了将原料的反应器入口温度控制在360℃至370℃的温度范围内,所有或一些进料气流或产物气流通过可调节阀(5),其中 以改变压力,从而改变冷凝温度。