• 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:
    The invention provides a process and the product of process for the preparation of N-phosphonomethyl-glycine comprising the oxidation of an aqueous suspension of N-phosphonomethyl-imino diacetic acid in the presence of a catalyst with oxygen or an oxygen-containing gas. Comparing the process of the invention with the known processes, specific conversion is considerably increased and significant amounts of energy can be saved.
    公开号:SU927121A3
    申请号:SU802917349
    申请日:1980-05-07
    公开日:1982-05-07
    发明作者:Гаал Антал；Фаркаш Йожеф；Хорват Шандор；Балинт Шандор；Колонич Золтан；Шолтес Ласло；Леринц Лайош；Хайду Петер；Ботар Ласло；Немеш Иштван；Гедра Агнеш；Шюмеги Ласло；Видроци Тамаш；Лукач Юлиа；Гал Деже；Кеслер Агнеш
    申请人:Нитрокемиа Ипартелепек (Инопредприятие)；
    IPC主号:
    专利说明:

    (5) METHOD FOR OBTAINING N-PHOSPHONOMETHYL GLYCINE
    one
    This invention relates to the chemistry of organophosphorus compounds, namely to an improved habitat for the production of N-phosphonomethylglycine, which can be used as a herbicide in agriculture.
    A known method for producing N-phosphonomethylglycine by the electrolytic oxidation of the tetraether of L-phosphonomethyliminodiacetic acid, followed by hydrolysis of the obtained product 1.
    Closest to the present invention is a method for producing N-phosphonomethylglycine by the catalytic oxidation of N-phosphonomethylaminodioacetic acid with oxygen or oxygen-containing gas at 70-120 ° C and a southeast pressure in the presence of an activated carbon catalyst with a specific surface equal to 300,100, taken as an amount by weight L-phosphonomethyl and diacetic acid 21.
    However, due to the poor solubility of N-phosphonomethylaminodiacetic acid, large quantities of aqueous solutions have to be processed, 5 this significantly reduces the useful production capacity of the reactor and increases energy costs. In addition, a large amount is removed from the waste solution.
    10 in water, which requires additional energy costs.
    The purpose of the invention is to simplify the process.
    The goal is achieved
    15 by the fact that in the method of obtaining N-phosphonomethylglycine, which consists in the fact that an aqueous suspension containing 7 to 70 g of N-phosphonomethylaminodiacetic acid in 100 ml of VO
    20 dyes are subjected to catalytic oxidation by oxygen or oxygen-containing gas at 70–120 ° C and pressure of 3 10 atm in the presence of a catalyst — activated carbon with
    "25 specific surface area equal to 300 3 190С, or platinum on activated carbon, or palladium on activated carbon, taken in a quantity of 5 by weight of N-phosphonomethylaminodiacetic acid, oxidation is carried out in an aqueous suspension containing 7 - / O g N-phosphonomethylaminodiacetic acids in 100 ml of water, and activated carbon, or platinum on activated carbon, or palladium on activated carbon is used as a catalyst. In this case, the oxidation is carried out in an aqueous suspension containing 20–50 g of Mphosphonomethyliminodioacetic acid in 100 ml of water. The proposed method is characterized by manufacturing methods, as it allows to exclude large quantities of aqueous solutions from the treatment, and also eliminates the need to remove large amounts of water from the waste solution, which reduces energy costs while simultaneously increasing the production and process. Example 1 (comparative). The reaction is carried out in a heated jacket, thermometer, valve for the supply and removal of gas by an acid-resistant steel tank made by rolling. A solution of 1 g of N-phosphonomethyliminoacetic acid in 100 water at 100 ° C is placed in the reactor, then O is added to the solution, and the catalyst in the form of activated carbon of Norit brand A. The reactor is closed, fixed on a shaking device, and compressed air is introduced into the reactor until the pressure reaches 6 atm. The reaction is carried out at 90-95 ° C with constant stirring. Formaldehyde and carbon dioxide formed during the reaction are bled out of the reactor every 30 minutes. Under these conditions, the reaction is completed in 2.5 hours, and 2.8 g of (100) pure S-phosphonome is obtained; tilglycine, the purity of which is confirmed by nuclear magnetic resonance spectroscopy data. The specific conversion is calculated according to the following equation: Weight of the final product, g Specific conversion Liquid volumes, lx Reaction time, 14 Conversion rate reached: 11.2 g / l h. Example 2. Proceed as described in Example 1, however 100 G of water and 20 g of N-phosphonomethylaminodiacetic acid, and 2 g of Norit A. as a catalyst. After 6.5 h of reaction, 1.5 gM -phosphonomethylglycine is obtained (, which corresponds to a specific conversion of 21.5 g / l h, which exceeds 1.9 times the value achieved in the comparative example. Example 3- Progress t, as described in example 1, however, 100 g of water, 40 g of N-phosphonomethylaminodiacetic acid are used as starting materials, and k catalyst Norita A is used as a catalyst. After 10 hours of reaction, 28.6 g (9, 7%) of N-phosphonomethylglycine are obtained, pure according to NMR spectroscopy. Achieved specific conversion: 28.6 g / l.h (2.5 times higher than in the comparative example). Example 4. Proceed as described in example 1, but the starting materials are 100 g water. 30 g of N-phosphonomethylaminodiacetic acid and 3 g of Norit A as a catalyst. After 8.5 hours of reaction, 21.2 g (93.6) of N-phosphonomethylglycine, pure according to NMR spectroscopy, are obtained. Specific conversion is achieved: 24.9 g / lh (2.2 times higher than in comparative example). Example 5. The reaction is carried out in an acid-resistant tank with a jacket for heating, equipped with a head-up mixing mixer and valves for supplying and discharging gas. 800 g of N-phosphonomethylaminodiacetic acid, 1000 ml of water and 30 g of Norit A catalyst are placed in an autoclave. The autoclave is closed, the reaction mixture is heated to 90 - and compressed air is supplied below the liquid level until the pressure reaches 6 atm. The suspension is stirred at a speed of 00 rpm. After the reaction, which lasts 8, -5 hours, 208 g (95.3%) of N-phosphonomethylglycine are obtained, purely by NMR spectroscopy. The specific conversion achieved: 2 g / lh is 2.2 times higher than in the comparative example.
    five
    After completion of the reaction, the catalyst is immediately filtered off, the residue is washed with hot water and dried at 110 ° C. The catalyst thus regenerated is used for subsequent syntheses.
    Example 6. Proceed as described in example 5, however, the source substances are 1000 ml of water, 200 g of N-phosphonomethyl aminodiacetic acid and as a catalyst 20 g Norita A.
    After 6.5 reactions, 6 g of () phosphonomethylglycine, pure according to NMR spectroscopy, is obtained. Achieved specific conversion: 22, g / l h (more than twice the value obtained in the comparative example).
    The catalyst is regenerated as
    described in example 5 and used for further operations.
    Example 7. Proceed as described in Example 1, however 100 ml of water, 20 g of N-phosphonomethyl, iminodiacetic acid are used as starting materials, 2 g of Norit A catalyst regenerated after the reaction of Example 6 are used as catalyst. 6.5 h of the reaction, k, 2 g is obtained (E, S% N-phosphonomethylglycine, pure according to NMR spectroscopy. A specific conversion is achieved: 21.8 g / l h (exceeding 1.9 times the value obtained in the comparative example).
    The catalyst is used for further five operating cycles. The activity of the catalyst does not decrease.
    Example 8. Proceed as described in Example 7, however, 100 ml of water, 120 g of N-phosphonomethylaminodiacetic acid and 2 g of catalyst in the form of palladium supported on Karbo C activated carbon are extra starting materials. After 5 hours of reaction, 1, () N-phosphonomethylglycine, pure according to NMR spectroscopy data. Conversion rate achieved: 28.8 g / l h (2.5 times greater than the value obtained in comparative example).
    Example 9- Proceed as described in Example 1, however, 100 ml of water and 20 g of N-phosphonomethyl 16 are used as starting materials.
    butylacetic acid and catalyst 2 g of Harbo Extra C activated carbon. After 7 hours of reaction, 1.3 g of () N-phosphonomethylglycine, pure according to NMR spectroscopy, is obtained. The specific conversion achieved: 20.8 g / l .4 (1.85 times the value obtained in the comparative example).
    Example 10. Proceed as described in example 1, but the starting materials are 100 ml of water,. 20 g of N-phosphonomethylaminodiacetic acid and a catalyst in the form of platinum supported on Carbo Extra C activated carbon. After 4.5 hours of reaction, I.Z g (SffSi) -phosphoromethylglycine, pure by NMR spectroscopy, is obtained. The specific conversion achieved: g / lh (2.8 times the value reached in the comparative example).
    PRI m 6 0 11. Proceed as described in example 2. As a catalyst, 8 g / 40 wt.% Is used as a reference to the starting material of Darko activated carbon X, the specific surface of which is 300 wVr. After the reaction, 13.5 g (90%) of NMR-spectroscopically pure N-phosphonomethylglycine is obtained. Unit conversion: g / lh (3 times more than was achieved in the comparative example).
    Example 12. Proceed as in example "2, but as a catalyst take C when correlated to the original substance / activated carbon Norit. The specific surface area of the catalyst is 1,100. Instead of air, pure gaseous oxygen was introduced into the suspension, and the reaction was carried out at 70 ° C. After 3 hours of reaction, 1 g (93.3) of NMR-spectroscopically pure N-phosphonomethylglycine was obtained. Unit conversion: k6.66 g / lh (“16 times more than achieved in the comparative example).
    Example 13. Doing as e. And in example 2, but as a catalyst using 1 g of activated carbon honey. Norit DAB UE in the amount of 5 wt.% In terms of the original substance. The catalyst surface area is 18001900 MVr. Air is introduced into the suspension containing kQ% oxygen. After
    权利要求:
    Claims (2)
    [1]
    Claim
    1. The method of producing N-phosphonomethylglycine by catalytic oxidation of N-phosphonomethyliminodiacetic acid with oxygen or an oxygen-containing gas at 70 ~ 120 ° C and a pressure of 3 “10 atm in the presence of a catalyst comprising activated carbon with a specific surface area of 300 - 1900 m 2 / g, 5 ~ 40% by weight of N-phosphonomethyliminodiacetic acid, characterized in that, in order to simplify the process, the oxidation is carried out in an aqueous suspension containing 7 ~ 70 g of N-phosphonomethyliminodiacetic acid in 100 ml of water, and use as a catalyst activated carbon, or platinum on activated carbon, or palladium on activated carbon.
    [2]
    2. The method of pop. 1, characterized in that the oxidation is carried out in an aqueous suspension containing 20 to 50 g of N-phosphonomethyliminodiacetic acid in 10Ϊ ml of water.
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    同族专利:
    公开号 | 公开日
    AT380687B|1986-06-25|
    ES491296A0|1981-04-01|
    PT71151A|1980-05-01|
    CS221969B2|1983-04-29|
    BR8002886A|1980-12-23|
    NO152416C|1985-09-25|
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    NL8002674A|1980-11-13|
    IN151845B|1983-08-13|
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    IE800944L|1980-11-11|
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    FI801363A|1980-11-12|
    HU184168B|1984-07-30|
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    JPS5618994A|1981-02-23|
    ATA247280A|1985-11-15|
    PL122706B1|1982-08-31|
    LU82380A1|1980-07-31|
    GB2049697B|1983-09-28|
    FI68242B|1985-04-30|
    IT8021972D0|1980-05-09|
    DE3063274D1|1983-07-07|
    YU42213B|1988-06-30|
    SE447901B|1986-12-22|
    FR2456115B1|1985-07-05|
    JPH025759B2|1990-02-05|
    NO152416B|1985-06-17|
    DK147144C|1984-10-08|
    YU124580A|1983-02-28|
    EP0019445B2|1988-10-05|
    EP0019445B1|1983-05-18|
    DD150614A5|1981-09-09|
    IE50347B1|1986-04-02|
    AU542716B2|1985-03-07|
    IL59903D0|1980-06-30|
    NO801381L|1980-11-12|
    DE3017518A1|1980-11-13|
    ES8104312A1|1981-04-01|
    PL224125A1|1981-02-13|
    DK147144B|1984-04-24|
    BG33276A3|1983-01-14|
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    BE883222A|1980-09-01|
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    SE8003396L|1980-11-12|
    NZ193573A|1982-11-23|
    IL59903A|1983-09-30|
    EP0019445A3|1981-06-03|
    AT3428T|1983-06-15|
    EG14671A|1986-09-30|
    CA1155138A|1983-10-11|
    ZA802456B|1981-04-29|
    EP0019445A2|1980-11-26|
    TR21105A|1983-09-01|
    AU5828580A|1980-11-13|
    GB2049697A|1980-12-31|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US3969398A|1974-05-01|1976-07-13|Monsanto Company|Process for producing N-phosphonomethyl glycine|US4442041A|1982-06-30|1984-04-10|Stauffer Chemical Company|Method for preparation of N-phosphonomethylglycine|
    IL68716A|1983-05-17|1987-03-31|Geshuri Lab Ltd|Process for producing n-phosphonomethylglycine|
    US4696772A|1985-02-28|1987-09-29|Monsanto Company|Amine oxidation using carbon catalyst having oxides removed from surface|
    US4582650A|1985-02-11|1986-04-15|Monsanto Company|Oxidation with encapsulated co-catalyst|
    US4579689A|1985-02-11|1986-04-01|Monsanto Company|Oxidation with coated catalyst|
    US4657705A|1985-09-23|1987-04-14|Monsanto Company|Process for the preparation of N-substituted aminomethylphosphonic acids|
    US4853159A|1987-10-26|1989-08-01|Monsanto Company|Process for producing N-phosphonomethylglycine|
    HU200780B|1988-02-08|1990-08-28|Nitrokemia Ipartelepek|Process for producing n-phosphonomethyl iminodiacetic acid from double salt of iminodiacetic acid|
    US4952723A|1989-07-31|1990-08-28|Monsanto Company|Process for producing N-phosphonomethylglycine|
    US5095140A|1990-06-25|1992-03-10|Monsanto Company|Peroxide process for producing N-phosphonomethylglycine|
    US5061820A|1990-10-22|1991-10-29|Monsanto Company|Process for producing N-phosphonomethylgylcine|
    SI9400449A|1994-12-20|1996-06-30|Pinus D D|Process for preparing N-phosphonomethyl glycin|
    US6417133B1|1998-02-25|2002-07-09|Monsanto Technology Llc|Deeply reduced oxidation catalyst and its use for catalyzing liquid phase oxidation reactions|
    PL364748A1|1999-07-23|2004-12-13|Basf Aktiengesellschaft|Method of producing glyphosate or a salt thereof|
    BR0111041A|2000-05-22|2004-06-15|Monsanto Technology Llc|Reaction systems for producing n-glycine compounds|
    US6921834B2|2002-05-22|2005-07-26|Dow Agrosciences Llc|Continuous process for preparing N-phosphonomethyl glycine|
    AR051926A1|2004-09-15|2007-02-21|Monsanto Technology Llc|OXIDATION CATALYSTS, PROCEDURES FOR THE PREPARATION OF SUCH CATALYZERS AND PROCESS FOR THE ELABORATION OF N-GLYCINE OR A SALT OF THE SAME|
    US8252953B2|2008-05-01|2012-08-28|Monsanto Technology Llc|Metal utilization in supported, metal-containing catalysts|
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    优先权:
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    HU79MA3146A|HU184168B|1979-05-11|1979-05-11|Process for producing n-bracket-phosphono-methyl-bracket closed-glycine|
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