• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Disclosed herein is a process for the hydration of a nitrile compound. Owing to the use of a Raney copper catalyst having an iron content of 0.7 wt. % or less based on the copper component in a suspended state, the process allows the catalyst to retain high activity and facilitates the separation of the catalyst and liquid reaction mixture by sedimentalion and/or filtration. In an example, a catalyst with 0.1 iron achieved 67% conversion of acrylonitrile to acrylamide, whereas a catalyst with 1.56% iron achieved only 40%.
    公开号:SU1575935A3
    申请号:SU853955956
    申请日:1985-09-19
    公开日:1990-06-30
    发明作者:Асано Сиро；Китагава Дзун
    申请人:Мицуи Тоатсу Кемикалз Инкорпорейтед (Фирма)；
    IPC主号:
    专利说明:

    The invention relates to organic chemistry, in particular to methods for producing amides, which can be used as monomers for the preparation of the corresponding polymers.
    The purpose of the invention is to simplify the process.
    The invention provides for the use of Rane’s skeletal copper catalyst having an especially low iron content. The main sources of iron that are mixed into the skeletal copper catalyst can be iron contained in aluminum, zinc used as soluble components in the Ren alloy, iron mixed as a result of wear or corrosion of steel equipment used in grinding or sifting.
    Rane to the required particle size, iron contained in sodium hydroxide and water, which are used to produce the Rane alloy, iron mixed as a result of wear or corrosion of the advanced processing equipment made of steel.
    To avoid a decrease in catalyst activity and a decrease in its filtration and filtration characteristics due to these various reasons, various counter measures must be taken to effectively minimize the ingestion of iron (use a limited number of grades and grades of aluminum or zinc to prepare the alloy, for example, the use of aluminum or zinc with a high iron content, reaching 0.4 wt.%; use equiped
    00
    oo ate

    cm
    for grinding and sieving, made of stainless steel instead of carbonaceous, use sodium hydroxide, which has the lowest possible iron content, and avoid changing the storage and storage equipment made of carbon steel; use soft water, deionize water as water and avoid the use of transport and storage equipment made of carbon steel; Use expansive stainless steel equipment.
    etc.).
    Due to the overall control parameters, you can use the skeletal catalyst Rene, having an iron content of 0.1-0.7 wt.%. Among these 20 different countermeasures, control of the iron and aluminum content and the choice of material for the equipment of the grinding and sifting systems are particularly important. If these countermeasures are not attempted, then a significant portion of iron remains in the Rane developed copper.
    The term reduced sedimentation characteristics means, for example, that after cessation of JQ injury, during the operation of a reactor equipped with a stirrer, the precipitation of suspended particles or grains of the skeletal copper-Fo catalyst Rane becomes more difficult.
    ,,.
    for example, in the reactor, by supplying a dividing wall to form the catalyst deposition zone (i.e., thickener), where turbulent flows do not act on the catalyst slurry, and the precipitated catalyst is recycled to the catalyst suspension zone, and the output mixture separated from the catalyst t from the reactor, this term means that the liquid reaction mixture thus withdrawn contains a greater amount of catalyst. which is still in a suspended state without being precipitated eniyu. Increasing the amount of this suspended catalyst means a direct loss of the effective amount of the catalyst, which leads to an increase in the consumption of the latter.
    On the other hand, the term reduced filtration characteristics means that the filtration resistance increases on the catalyst filter.
    0 5
    Q
    five
    five
    designed inside or outside the reactor. This phenomenon leads to a decrease in productivity.
    Example 1. A 1: 1 alloy of copper and aluminum is milled and sieved to produce a René copper alloy having a particle size of less than 80 mesh (0E175 mm). The alloy powder is developed in the usual way with sodium hydroxide followed by thorough washing with water to prepare a Ren skeleton copper catalyst. “Among a number of catalyst lots obtained by the indicated,. In this way, batches are used in which the iron content is 0.10E 0524, 0.41, 0.70, 1.15, and 1956% in terms of their copper components. The analysis of the iron content is carried out using atomic absorption spectroscopy after dissolving the catalysts in nitric acid.
    The iron content of the Rane alloys chosen in this way from six different batches before grinding and sieving, as well as for the material used in the mill, is given in Table. one .
    Tests carried out in a periodic mode using these six catalysts from different batches. A flask per 100 ml equipped with a stirrer, thermometer and reflux condenser was charged with 6.6 g of acrylonitrile, 36 g of water and 7 g of one of the catalysts. Since the catalyst is prepared and stored in the water in suspension; when the catalyst is loaded, about 7 g of water is also supplied. Thus, this value is previously subtracted from the separately charged amount of water, so that the total amount of water is 36 g 0
    The flask is heated outside in the bath to a temperature of about 70 ° C. Thereafter, the reaction is carried out for 2 hours, regulating the temperature of the bath to maintain the internal temperature in the flask at a level.
    Possible dissolved oxygen is removed from the raw materials in advance. In subsequent operations, air penetration is avoided to avoid contact of the catalyst with oxygen. After 2 hours, the flask is cooled to stop the reaction and the liquid reaction mixture is analyzed by gas chromatography to determine
    conversion of acrylonitrile to acrylamide. The results are shown in Table. one.
    When the Rane skeletal copper catalyst is used for the industrial production of acrylamide, its conversion is preferably 60% and higher in the described activity test. From the data of Table 1, it can be concluded that the iron content should be about 0.1-0.7% by weight in order to achieve such a conversion.
    Example 2. Using the three catalysts of Example 1, which have an iron content of 0.24, 0.70 and 1.56%, respectively, the following tests are carried out in a continuous mode of reaction management.
    150 parts of one of the catalysts are loaded into a stainless steel reactor equipped with a stirrer and an integrated catalyst filter, and charged with costs of 300 and 700 mash. at 1 hr, respectively, acrylonitrile and water, from which possible dissolved oxygen was previously removed by blowing nitrogen gas. The reaction is carried out at 120 ° C with simultaneous stirring of the reaction mixture to maintain the catalyst in a suspended state. As a reaction promoter, copper nitrate is added to the feed water in such a quantity that its concentration reaches 20 calculated from the liquid reaction mixture as measured by nitrate radicals.
    The liquid reaction mixture flows through the catalyst filter, and then it is withdrawn from the reactor as a liquid free from catalyst. After that, it flows into a sealed tank for the reaction liquid. It is taken from the tank once a day.
    Samples are taken from the liquid reaction mixture that flows out of the reactor every two days, and analyzed by gas chromatography to determine the conversion of acrylonitrile to acrylamide.
    The pressure in the tank for the reaction liquid is always maintained at 4 kgf / cm2 (g) by pressurization or nitrogen gas release. Thus, the reactor has a pressure slightly higher than 4 kgf / cm2. This
    the pressure difference (RR) indicates mainly the resistance of the filtration zone of the catalyst filter.
    ZIP value is close to 0 in the first day of the reaction. It begins to increase as the reaction proceeds. The reaction is stopped when dP exceeds 2 kgf / cm2.
    The test results are shown in Table. 2 and 3. More specifically, the high conversion and lower PD values are maintained for a test period of 14 days, for
    5 of which use a catalyst having a reduced iron content. However, when using a catalyst with a high iron content, the conversion remained low, and 4P increased at an earlier stage of testing, which led to its cessation.
    The experiment described was repeated, except that the iron content was changed to 1.40%, and iron nitrate (Fe (N03) 3) was added to the feed water in such an amount that the concentration reached 3 and 200 ppm of liquid reaction medium when measuring x
    0 based on nitrate radicals. The results are shown in table 4 and 5 (experiments 2-4 and 2-5).
    Further, the above experiment was repeated with the exception that
    5, the amount of catalyst was reduced to 75 hours and the reaction was conducted at 140 ° C. The results are shown in table 4 and 5 (experiment 2-6).
    Example Using the same 6
    0 catalysts from different batches, as in example 1, are tested under the reaction conditions according to the method of example 1, except that methacrylonite is used instead of acrylonitrile. 6
    Example 4. Using the same 3 catalysts from different batches as in example 2, tests were performed by reacting under conditions of a continuous flow mode as described in example 2, except that methacrylonitol-RIL was used instead of acrylonitrile.
    The results are presented in table.7 and 8.
    Example 5. Using the same 6 catalysts from different batches as
    in example 1, tests are carried out under the conditions of the reaction according to the method of example 1, except that cotinonitrile is used instead of acrylonitrile.
    The results are shown in Table. 9 Thus, the advantages of the process are achieved by carrying out a process using a Rane skeletal copper catalyst capable of maintaining high activity over a long service life when the nitrile compound is reacted with water in the presence of Rane's skeletal i copper catalyst to obtain the corresponding amide acid .
    In addition, the proposed method allows the use of a catalytic system that exhibits the best sedimentation-filtration characteristics of tics when carrying out the reaction in the presence of a René skeletal copper catalyst in a suspended state, followed by separation of the catalyst from the liquid reaction mixture. and filtering.
    权利要求:
    Claims (1)
    [1]
    Invention Formula
    The method of producing amides by the hydration of a nitrile selected from the group of acrylonitrile, methacrylonitrile or nicotinonitrile, in the presence of a copper catalyst Rane in suspension, containing aluminum and copper in a ratio of 1: 1 and iron, in a sealed reactor at a mass ratio of nitrile to water 15.5-60; 45-84.5E 70- 140 ° C, at a conversion of 10-98%, characterized in that in order to simplify the process, use of a skeletal catalyst Rane containing iron in an amount of 0.1-0.7 May , 7, in terms of the copper component.
    Table 1
    0, 04
    Note. Stainless steel — SUS 304 steel was used, carbon steel — SS4K steel was used. Each of the six experiments showed selectivity of acrylonitrile to acrylamide of more than 99.5% with a very small amount of α-oxy-progzonitrile, p-oxpropionamide and acrylic acid as the main secondary products.
    sua
    72 67 64
    LTD
    Table2
    51 46 42
    About About 0.4
    Note,
    In each of the three experiments, the same major by-products as in Example 1 were found in the reaction liquid, and they increased day by day during the experiment based on the acrylamide obtained. Thus, the selectivity for each experiment was about 99.7% on the first day and about 99.4% on the last day. There was no significant difference in selectivity in the three experiments.
    Table3
    Continuation of table 2
    example
    Ln j
    (l
    Cho
    U3 1L
    Note. In each of the six experiments was
    selectivity of methacrylonitrile to methacrylamide more than 99.5% was obtained.
    Table
    Table
    171 165
    158,152,145
    Comparative example
    Note. Each experiment showed a change in selectivity, as in
    measure 2, thus 5 the selectivity for each experience was 99.8% on the first day and about 99.5% on the last day. Significant differences in selectivity in the three experiments were not observed,
    Table9
    Table
    at
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    同族专利:
    公开号 | 公开日
    JPS6176447A|1986-04-18|
    ZA856934B|1986-04-30|
    AT55766T|1990-09-15|
    EP0175581A2|1986-03-26|
    CA1227488A|1987-09-29|
    ES8605751A1|1986-04-01|
    AU561379B2|1987-05-07|
    EP0175581A3|1987-05-20|
    BR8504588A|1986-07-15|
    DE3579280D1|1990-09-27|
    AU4730985A|1986-03-27|
    KR860002457A|1986-04-26|
    KR870001678B1|1987-09-22|
    ES547124A0|1986-04-01|
    EP0175581B1|1990-08-22|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3944609A|1973-06-01|1976-03-16|American Cyanamid Company|Catalyst preparation method|
    AU471081B2|1973-10-12|1976-04-08|Method of producing olefinic amides with a raney copper catalyst|
    JPS5233612B2|1973-12-21|1977-08-30|JPH0662527B2|1985-03-27|1994-08-17|三井東圧化学株式会社|Method for producingacrylamide|
    EP0246813B1|1986-05-21|1991-01-16|Ciba Specialty Chemicals Water Treatments Limited|Catalysts and their use in the hydrolysis of nitriles|
    CA2087557C|1992-07-31|2000-04-25|Matthew Raskin|Method for removing catalyst|
    EP1382388A1|2000-02-18|2004-01-21|Degussa AG|Fixed-bed copper Raney catalyst for dehydrating alcohols|
    EP1382389A1|2000-02-18|2004-01-21|Degussa AG|Raney copper catalyst for the dehydrogenation of alcohols|
    US20020038051A1|2000-02-18|2002-03-28|Degussa-Huls Ag|Raney copper|
    WO2012017966A1|2010-08-02|2012-02-09|国立大学法人岡山大学|Metal complex compound and amide production method that utilizes said metal complex compound|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    JP59195721A|JPS6176447A|1984-09-20|1984-09-20|Hydration of nitrile compound|
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