• 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:
    Electrolytic reduction of tetrachloro-2-picolinic acid in basic aqueous solution, at an activated silver cathode, yields the 3,4,6- and 3,5,6-trichloro-2-picolinic acids, which in turn may be further reduced to 3,6-dichloropicolinic acid, a highly active herbicide.
    公开号:SU1077568A3
    申请号:SU802940707
    申请日:1980-07-01
    公开日:1984-02-29
    发明作者:Куриаку Деметриос；Ешихиро Едамура Фред；Лав Джим
    申请人:Дзе Дау Кемикал Кампани (Фирма)；
    IPC主号:
    专利说明:

    H VI
    : l

    thirty
    This invention relates to a process for the preparation of 3, b-dichloropicolinic acid, which is used in agriculture as a plant growth regulator.
    A known method for the preparation of 3,6-dichloropicolinic acid (3,6-D), which consists in the fact that tetrachlolikolinov is. the acid is reacted with hydrazine hydrate in the presence of sodium carbonate and the resulting 3,5,6-trichloro-4-hydrazine picolinic acid is boiled with sodium hydroxide in an aqueous-alcoholic medium, followed by cooling the reaction mixture and treatment with concentrated hydrochloric acid. Target product yield 53 | l o
    The disadvantages of this method are the low yield of the product and the multistepness, which complicates the process.
    The purpose of the invention is to increase the yield of the target product and simplify the process technology.
    This goal is achieved in that tetrachloropicolinic acid is subjected to electrochemical reduction at a cathode consisting of silver microcrystals in an alkaline medium at an alkali concentration of 0.1-3.75 g / mol, the cathode potential relative to the standard calomel electrode -0.8 - 1, 8.V and temperature.
    This allows to obtain the target product with a yield of more than 90%.
    Laboratory experiments on the reduction of tetrachloro-2-picolinic acid (tet-acid) to 3, b-dichloropicolinic acid (3, b-C) using a cathode activated on site.
    Example 1. Electrolyzer A, In a beaker (capacity 300 Mn equipped with a magnetic stirrer, put a solution of 15 g of sodium hydroxide tablets of reactive purity in 150 ml of distilled water. A flat (57.5 cm) cathode of silver mesh is immersed in the upper part of the solution 20 mesh (0.84 mm orifice diameter), a saturated calomel comparison electrode, and (1 cm from the cathode) a graphite plate anode (5-7.5 cm 2 mm). After turning on the stirrer, connect the cathode and the anode to a constant source. current and injected into a stirred solution of 3 ml of water containing 60 mg of silver nitrate. The potential of the cathode in relation to the reference electrode is maintained at –1.3 V, and the cell voltage is set (at 2 V) so that the initial current is Z. 10 g of tet-acid added over
    30 Min for 4.5 hours at a temperature of about 25 C, the force exponentially falling. to less than 0.3 A and the reduction is terminated. By acidification (25 ml of concentrated hydrochloric acid), extracted with dichloromethane and evaporation of the extract from the electrolytic solution, 6.8 g of a white solid were isolated according to spectroscopy and gas chromatography analysis contains 92.2 wt.% 3,6-D.
    Example 2. The test was carried out as in Example 1, with the exception that silver nitrate was not added, and the cathode was activated by repeated polarity reversal (several times per cycle with the stirrer switched on). As a result, 7.2 g of crude product (yield, $ 7.9% of theory) containing 91% of 3,6-Dc was recovered.
    Example 3. The test was carried out as in Example 2, but after converting 95% of the initially taken tet-acid, another 10 g of tetra-acid and 3 g of sodium hydroxide were introduced into the electrolyzer and the electrolysis was continued until the total duration of the process was 9 hours. The result of 14.6 g (yield of 99.3%) from the theory of the crude product with a content of 3,6-D 91,4 wt.%.
    In this experiment, the total molar ratio of tet-acid to sodium hydroxide is 0.17, and the final OH / C1 ratio, approximately calculated under the assumption that 3,6-D is the only reaction product, is 1.7. The final weight concentration of sodium hydroxide in the reaction mixture is approximately 5.1% (if we take into account the weight of hydrogen and oxygen introduced during the reaction, this value will be slightly higher value).
    Example 4. Six experiments (a-i) were carried out using a 20 mesh silver mesh cathode. The cathode is activated by means of anodes oxidation, i.e. according to the method described in example 2. The cathode with a diameter of about 7 cm is installed vertically so that it surrounds the lamellar graphite anode (5-7.5 cm-2 mm). A potentiostat was used as a source of direct current (Prinstone’s model 317 model). The electrolyzer (a chemical beaker with a capacity of 300 or 600 m, depending on the volume of the reaction mixture) is partially immersed in a thermostatically controlled water bath. The saturated calomel electrode in the Luggin capillary is mounted so that the end of the capillary barely touches the cathode. Stirring is carried out using a magnetic stirrer installed under the water bath and
    magnetic rod placed in solution.
    In tab. Table 1 shows the quantities of reagents taken, the reaction conditions, the duration of the process, the yield and purity of the product 3,6-D, isolated by acidification, extraction and evaporation.
    It should be noted that the final OH / C1 ratios given in Table. 1, are the theoretical minimum attitudes calculated on the assumption of 100% conversion of Tet-acid to 3,6-D.
    Example 5. A series of three experiments (o - c) on restoring the tetradscuts was carried out according to the procedure described in Example 4, with the exception that the silver grid used as a cathode is coated with silver by means of cathodic polarization in 14 silver nitrate solution.
    Three additional experiments (d -i were performed in an anxogogic way, but using silver-coated monelon mesh cathodes (d and e) and a silver-plated nickel mesh (i).
    As a result of the collection and analysis of gases separated on the electrodes during these experiments, it was found that the rate of oxygen supply (at the cathode) is close to the theoretical value calculated for the total reaction, and 10-15 times higher than the rate of hydrogen evolution (at the anode).
    The results of these. Six experiments are given in table. 2
    Example 6 A series of 4 runs (o-d) was performed with different assignments of tet-acid to sodium hydroxide using a preliminary, but purified and activated in place, silver mesh cathode, which is periodically reactivated during reduction.
    To a 300 ml of distilled water in a 680 mp beaker is added (with stirring with a magnetic stirrer and a predetermined temperature / water bath) a predetermined amount of sodium hydroxide of reactive purity grade. An alkaline solution formed completely immersed the flat electrode (5 7.5 cm) of 20 mesh silver mesh (hole diameter 0.84 mm).
     The electrode is preliminarily kept for 10 min in a mixture of water with concentrated hydrochloric acid (1: 1) and lroked with water. In an alkaline solution at a distance of 1 cm from the cathode, a flat graphite anode, having the same dimensions as the cathode, is pressed. A positive potential is applied to the cathode (relative to the saturated calomel electrode of comparison), which is hardly detectable at the beginning of the experiment. within a few minutes, it rises to +0.6 V. Then, the switching voltage is made and the cathode potential is set at about –1.3 V (cell voltage of about 2 V). 5 g of tet-acid is mixed with 20 ml of an alkaline solution taken from an electrolyzer, and the resulting suspension is returned to the electrolyzer, thus starting the reduction. This procedure is repeated until (2 hours) until the entire
    5 sample (35 g) of tet-acid to be reduced. Thereafter ; the cathode is reactivated by changing the polarity (up to +0.6 B) for approximately 3 minutes. VosQ formation continues to the total reaction time of 8 hours, the cathode is reactivated every 2 hours. The current of the cell increases from the initial value.
     about 3 A approximately
    to 5 A at the time when the alkaline solution becomes saturated with the sodium salt of the tet-acid, and then decreases to a final value of approximately 0.3 A.
    0
    The contents of the electrolyzer are treated by acidification, triple extraction with dichloromethane and evaporation (it has been found that when using an insufficient amount of dichloromethane, an emulsion is formed at the first extraction extract, which is easily destroyed by the addition of dichloromethane).
    The results of these four experiments are given in Table. 3
    The implementation of the proposed method on a pilot plant Stan dratny electrolyzer, condition, method. The rectangular case with outer dimensions of 5.12513 "48 inches (13-33-122 cm) is mounted from two lucite support plates 113-48 inches (7.6-33-122 cm).
    pre-slime raml
    313-48 lumens (7.6-33-122 cm) made of lucite plates 1 inch thick (2.54 cm) with two rectangular neoprene pads
    5 1/16 inch thick 0.16 cm and
    1 inch (2.54 cm) wide and 40 bolts 3,, 5 or 3.8 "1.75 inches (0.95-3.8 or 0.95-4.4 cm), to the inner surface of one of two
    0 support plates are attached to the ten; 9/16 inch (1.44 cm) silver plated Monel bolts evenly placed, fitted with individual gaskets, 20-mesh flat silver mesh (hole diameter, and 84 mm) with dimensions of 40 inches (0.16.27.6-102 cm ). Similarly, in a graphite anode with dimensions of 40 inches (7 "27.6-102 cm), ten equally spaced holes are drilled, an internal reeb is cut into them and the anode is attached to the inner surface of the second support plate with rhodium-coated titanium bolts. Between the anode and the cathode leaves a gap of 1/4 inch (0.635 cm). The top and bottom openings of the electrolyzer (box) are connected to circulate fluid in the system including electrolysis (upstream small heat exchanger, funnel (to add reagents) and centrifugal pump. A saturated calomel electrode (in the Luggin capillary) is injected through a special hole in the lid of the electrolysis cell and set it so that it barely touches the cathode. The power source for the electrolysis cell is a metal rectifier of the firm General Electric (0-10 V, 07500 A) reversibly connected to Strike parts of the cathode and anode bolts. Silver on the grid, which is used in most experiments, is pre-coated (in place) silver. To do this, (The electrolyzer is filled with a solution of 36 g of silver nitrate in approximately 5000 ml of 19% aqueous solution of NH40H and wire t cathode polysilization of the grid (potential from -0.05 to 0.13 V relative to the saturated calomel electrode, 16 A) for 90 minutes, drain the liquid from the electrolyzer and wash it 4 times with distilled water. The electrolysis cell is 4 liters, and the total volume of the sistek is about 23 J. Before each experiment, the entire washing system is clean. For cleaning, the electrolyzer in all the glasses, except for those specifically mentioned, is filled for a few minutes with a mixture of water with concentrated hydrochloric acid (Isl), and then the liquid is drained. Thereafter, the system is again run out, sodium hydroxide and water are charged, and the alkaline solution is circulated temporarily for a short time. When the pump is on, gradually (in a few minutes) the cathode potential increases from O to +0.6 V (relative to the electrode), and the rectifier voltage is set in such a way as to maintain such a cathode potential for several. minutes Then, the polarization of the electrolyzer is gradually changed to establish a cathode potential of –1.3 V (total activation time is about 10 minutes). In the experiments, either a tableted sodium hydroxide of a reactive purity grade or a 50% caustic from a mercury cell was tested. The alkali is dissolved in purified water or diluted with purified water in such a ratio so as to provide the specified initial content of sodium hydroxide in the reaction mixture (about 6-7 wt.%). A portion of tet-acid (purity not less than 97%) is mixed with a portion of the alkaline solution taken from the funnel, the mixture is treated in a Caules disperser and returned to the funnel. After that, the pump is turned on and the mixture of tet-acid and caustic is started to circulate through the electrolyzer at a speed of .38–95 L / min and, consequently, the reduction process about the temperature of the reaction mixture is measured at a point between the bottom of the electrolyzer and the heat exchanger, and maintained within the prescribed limits by controlling the flow of cooling water, flows to the heat exchanger. Tet-acid in a weight ratio of 0.8-1.6 to sodium hydroxide introduced into the reaction system. The subsidence current of the electrolysis cell varies between 98 and 188 A, which corresponds to nominal current densities of 0.036-0.056 A / cm, if the area of the exposed part of the cathode surface is 10 7 40 435 square inches or 1, 4 cm. is a grid, in fact, the current density ranges between 05 and 0.07 A / cm. The initial current of the electrolyzer is high (up to 315 A), but during recovery it decreases, it could reach (depending on temperature) 16 A. immediately after the experiment was over. The reaction was followed by periodically sampling the electrode content (system) and potentiometric titration wire 0.1N silver nitrate solution to determine the chloride ion content. When the growth rate of the chloride ion content becomes very low and their current efficiency decreases to a minimum, the reaction is stopped and the liquid is drained from the installation. The composition of the reaction mixture is determined by gas chromatography. A sample (150 ml) of the reaction mixture, which is usually a homogeneous aqueous plant. the thief is acidified to pH 1 and extracted three times with dichloromethane. The extracts are combined, dried over sodium sulfate, and evaporated on a rotary evaporator at 45 bos. The resulting solid or semi-solid residue is dried in vacuum for 1 hour, cooled and weighed. The product suspension (approximately 0.1 t 7 mixed with the same weight 1,2,3, 4-tetrachlorobenzene (internal stan dard) and 1 ml of NI 0-Bic (trimethylsilyl) acetamide. The resulting mixture is heated in the reactor Reactiter, (Pierce Keikal), for 10-15 minutes at 60 ° C dl: converting various picolinic acids to the corresponding trimethylsilyl ether Then the mixture is introduced into: a gas chromatograph and the separation is carried out with a programmed temperature increase from. The detection is carried out by the thermal conductivity difference. The chromatographic characteristics of several expected components of the sample are determined in advance on pure reference substances. Example 7. Preparation of 3,6-D, The basic data on nine experiments (d- - i) / carried out according to the method discussed above are given in Table 4 o. When calculating yields, the theory assumes a not quite strict assumption that total weight loss is reactive oh mixture is due only to the release of oxygen. The purity of the starting tet-acid is assumed to be equal to 97%, although sometimes it reaches 97.9%. This is due to the lack of reliable analysis results of all used tet-acid batches. Given this fact, the apparent 100% yields (or higher) achieved in some experiments are presented in table. 4 maximum value of 99%. In some experiments, in addition to the content of 3,6-D in the final product, the concentrations of tet-acid, trichloropicolinic acids, monochlorine, .4,5-dichloro- and 4-hydroxy-3,5, b-trichloroicolinic acids are determined. However, the content of these impurities is low; therefore, the corresponding data in Table 4. not presented. Theoretically, the minimum numerical ratio calculated for each of the experiments presented in Table. 4, is approximately equal to 0.6, and the actual values of the final ratio, found analytically, show good agreement with this value. Table
    e200 208.33 208.33 .0.153
    t15012 6.98 105.81 1,128
    -1.3-1, 6
    1.76. -1,6
    TO -1.8
    2.42
    26
    0.3
    1.6
    The formation of ions Sat and OSG. “Excess hydrogen distribution (at the cathode). The current output is about 90%.
    Continuing taE5l. one
    version 50%
    91
    99
    Table Notes
     Purity of about 97%, yields sootvetstvimim way.
    adjusted.
     The theoretical minimum OH / CL ratio calculated on the assumption of 100% tet-acid conversion to 3,6-D.
    23170
    9.8
    6.3
    23170 9.8 6.3
    Continued table. 2
    Table 4
    - -1.28
    9-37-1.28 20-35 e. The current efficiency in experiment 5q is about 85%, and in each of the experiments -f it is about 80%. The theoretical minimum ratio calculated on the assumption of complete tet-acid conversion to 3,6-D. Table
    Table. four
    权利要求:
    Claims (1)
    [1]
    METHOD FOR PRODUCING 3,6-DICHLOROPICOLIC ACID using tetrachloropicolinic acid, characterized in that, in order to increase the yield of the target product and to 'simplify the process technology, tetrachlorocholinic acid is subjected to electrochemical reduction on a cathode' consisting of silver microcrystals, medium with an alkali concentration of 0.1-3.75 g / mod, cathode potential with respect to the standard calomel electrode ^ -0.8 - -1.8 V and a temperature of 5-60 ° C.
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    同族专利:
    公开号 | 公开日
    DE3068297D1|1984-07-26|
    IL59928D0|1980-06-30|
    EP0023077B1|1984-06-20|
    IN152627B|1984-02-25|
    GB2056492B|1983-04-27|
    KR830002711A|1983-05-30|
    KR840000447B1|1984-04-07|
    AR225441A1|1982-03-31|
    EP0023077A3|1981-06-03|
    UA6322A1|1994-12-29|
    ZA802659B|1981-07-29|
    ES8106564A1|1981-07-01|
    HU182150B|1983-12-28|
    AU5799080A|1981-01-15|
    DK152591B|1988-03-21|
    JPS569382A|1981-01-30|
    BR8004103A|1981-01-27|
    JPS6249357B2|1987-10-19|
    EP0023077A2|1981-01-28|
    NZ193544A|1983-06-14|
    ES491777A0|1981-07-01|
    MY8500086A|1985-12-31|
    IL59928A|1984-02-29|
    CA1142877A|1983-03-15|
    AU529604B2|1983-06-16|
    DD152366A5|1981-11-25|
    GB2056492A|1981-03-18|
    DK229680A|1981-01-03|
    DK152591C|1988-09-12|
    US4217185A|1980-08-12|
    CS222175B2|1983-05-27|
    引用文献:
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    US3971799A|1974-12-27|1976-07-27|The Dow Chemical Company|Preparation of 3,5,6-trichloropicolinic acid|US4334074A|1981-02-02|1982-06-08|The Dow Chemical Company|Method of recovering 3,6-dichloropicolinic acid from basic aqueous solutions of salts thereof|
    US4592811A|1981-09-28|1986-06-03|The Dow Chemical Company|Electrolytic cell comprising stainless steel anode, basic aqueous electrolyte and a cathode at which tetrachloro-2-picolinate ions can be selectively reduced in high yield to 3,6-dichloropicolinate ions _|
    US4533454A|1981-09-28|1985-08-06|The Dow Chemical Company|Electrolytic cell comprising stainless steel anode, basic aqueous electrolyte and a cathode at which tetrachloro-2-picolinate ions can be selectively reduced in high yield to 3,6-dichloropicolinate ions|
    US4460441A|1982-08-31|1984-07-17|The Dow Chemical Company|Expanded metal as more efficient form of silver cathode for electrolytic reduction of polychloropicolinate anions|
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    JPH0670277B2|1984-06-14|1994-09-07|ザ・ダウ・ケミカル・カンパニー|Expanded metal silver electrode for electrolytic reduction of polychloropicolinate anion|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US06/054,130|US4217185A|1979-07-02|1979-07-02|Electrolytic production of certain trichloropicolinic acids and/or 3,6-dichloropicolinic acid|
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