WO2009079862A1 - New preparation method of glyphosate by oxidation pmida with air - Google Patents
New preparation method of glyphosate by oxidation pmida with air Download PDFInfo
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- WO2009079862A1 WO2009079862A1 PCT/CN2007/003774 CN2007003774W WO2009079862A1 WO 2009079862 A1 WO2009079862 A1 WO 2009079862A1 CN 2007003774 W CN2007003774 W CN 2007003774W WO 2009079862 A1 WO2009079862 A1 WO 2009079862A1
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- Prior art keywords
- glyphosate
- activated carbon
- reaction
- air
- carbon nanotubes
- Prior art date
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- 239000005562 Glyphosate Substances 0.000 title claims abstract description 93
- 229940097068 glyphosate Drugs 0.000 title claims abstract description 93
- XDDAORKBJWWYJS-UHFFFAOYSA-N glyphosate Chemical compound OC(=O)CNCP(O)(O)=O XDDAORKBJWWYJS-UHFFFAOYSA-N 0.000 title claims abstract description 92
- 230000003647 oxidation Effects 0.000 title claims abstract description 32
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 32
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 107
- 238000000034 method Methods 0.000 claims abstract description 64
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 20
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 20
- 239000001301 oxygen Substances 0.000 claims abstract description 20
- 239000002041 carbon nanotube Substances 0.000 claims abstract description 14
- 229910021393 carbon nanotube Inorganic materials 0.000 claims abstract description 14
- 238000006243 chemical reaction Methods 0.000 claims description 65
- 239000007789 gas Substances 0.000 claims description 7
- 239000010970 precious metal Substances 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 3
- 239000002184 metal Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 2
- 239000003575 carbonaceous material Substances 0.000 claims 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims 1
- 230000001939 inductive effect Effects 0.000 claims 1
- 229910010272 inorganic material Inorganic materials 0.000 claims 1
- 239000011147 inorganic material Substances 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 35
- 239000003054 catalyst Substances 0.000 abstract description 29
- AZIHIQIVLANVKD-UHFFFAOYSA-N N-(phosphonomethyl)iminodiacetic acid Chemical compound OC(=O)CN(CC(O)=O)CP(O)(O)=O AZIHIQIVLANVKD-UHFFFAOYSA-N 0.000 abstract description 23
- 230000008901 benefit Effects 0.000 abstract description 8
- 230000001590 oxidative effect Effects 0.000 abstract description 8
- 239000007800 oxidant agent Substances 0.000 abstract description 7
- 239000003638 chemical reducing agent Substances 0.000 abstract description 2
- 239000003570 air Substances 0.000 description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 21
- 239000000843 powder Substances 0.000 description 20
- 239000000243 solution Substances 0.000 description 20
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 12
- 230000003197 catalytic effect Effects 0.000 description 12
- 229910052698 phosphorus Inorganic materials 0.000 description 12
- 239000011574 phosphorus Substances 0.000 description 12
- 238000003756 stirring Methods 0.000 description 11
- 239000000047 product Substances 0.000 description 9
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Chemical compound NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 description 6
- 230000008034 disappearance Effects 0.000 description 6
- NBZBKCUXIYYUSX-UHFFFAOYSA-N iminodiacetic acid Chemical compound OC(=O)CNCC(O)=O NBZBKCUXIYYUSX-UHFFFAOYSA-N 0.000 description 6
- 238000001228 spectrum Methods 0.000 description 6
- 229910052723 transition metal Inorganic materials 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000001514 detection method Methods 0.000 description 5
- 229910000510 noble metal Inorganic materials 0.000 description 5
- 150000003624 transition metals Chemical class 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 239000004471 Glycine Substances 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical group C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 239000004009 herbicide Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 229910017116 Fe—Mo Inorganic materials 0.000 description 2
- 108010008488 Glycylglycine Proteins 0.000 description 2
- -1 N-(phosphonocarboxyl)-glycine Chemical compound 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- XYFCBTPGUUZFHI-UHFFFAOYSA-N Phosphine Chemical compound P XYFCBTPGUUZFHI-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- HYBBIBNJHNGZAN-UHFFFAOYSA-N furfural Chemical compound O=CC1=CC=CO1 HYBBIBNJHNGZAN-UHFFFAOYSA-N 0.000 description 2
- 230000002363 herbicidal effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- 239000002048 multi walled nanotube Substances 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- 239000013110 organic ligand Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- XMVONEAAOPAGAO-UHFFFAOYSA-N sodium tungstate Chemical compound [Na+].[Na+].[O-][W]([O-])(=O)=O XMVONEAAOPAGAO-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 229940122361 Bisphosphonate Drugs 0.000 description 1
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- AMAFLHJIOPLMSA-UHFFFAOYSA-N [C].OO Chemical class [C].OO AMAFLHJIOPLMSA-UHFFFAOYSA-N 0.000 description 1
- 230000001133 acceleration Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000003862 amino acid derivatives Chemical class 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 150000004663 bisphosphonates Chemical class 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 150000004696 coordination complex Chemical class 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- XQRLCLUYWUNEEH-UHFFFAOYSA-L diphosphonate(2-) Chemical compound [O-]P(=O)OP([O-])=O XQRLCLUYWUNEEH-UHFFFAOYSA-L 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910001448 ferrous ion Inorganic materials 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000007172 homogeneous catalysis Methods 0.000 description 1
- XEMZLVDIUVCKGL-UHFFFAOYSA-N hydrogen peroxide;sulfuric acid Chemical compound OO.OS(O)(=O)=O XEMZLVDIUVCKGL-UHFFFAOYSA-N 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 238000004811 liquid chromatography Methods 0.000 description 1
- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 230000005501 phase interface Effects 0.000 description 1
- XYFCBTPGUUZFHI-UHFFFAOYSA-O phosphonium Chemical compound [PH4+] XYFCBTPGUUZFHI-UHFFFAOYSA-O 0.000 description 1
- 229910000073 phosphorus hydride Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229940001584 sodium metabisulfite Drugs 0.000 description 1
- 235000015393 sodium molybdate Nutrition 0.000 description 1
- 239000011684 sodium molybdate Substances 0.000 description 1
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- ISIJQEHRDSCQIU-UHFFFAOYSA-N tert-butyl 2,7-diazaspiro[4.5]decane-7-carboxylate Chemical compound C1N(C(=O)OC(C)(C)C)CCCC11CNCC1 ISIJQEHRDSCQIU-UHFFFAOYSA-N 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
- A01N57/00—Biocides, pest repellants or attractants, or plant growth regulators containing organic phosphorus compounds
- A01N57/18—Biocides, pest repellants or attractants, or plant growth regulators containing organic phosphorus compounds having phosphorus-to-carbon bonds
- A01N57/20—Biocides, pest repellants or attractants, or plant growth regulators containing organic phosphorus compounds having phosphorus-to-carbon bonds containing acyclic or cycloaliphatic radicals
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/28—Phosphorus compounds with one or more P—C bonds
- C07F9/38—Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
- C07F9/3804—Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)] not used, see subgroups
- C07F9/3808—Acyclic saturated acids which can have further substituents on alkyl
- C07F9/3813—N-Phosphonomethylglycine; Salts or complexes thereof
Definitions
- the invention relates to a novel process for catalytic oxidation of glyphosate to synthesize an important pesticide-herbicide glyphosate.
- Glyphosate (glyphosate, N-(phosphonocarboxyl)-glycine) is a herbicide selected by Monsanto Chemical Company in the 1960s and belongs to amino acid derivatives. The good biological activity of glyphosate makes it a highly effective, low-toxic, post-emergence herbicide for a wide range of applications. Currently, annual sales rank first among pesticide products.
- the synthesis methods of glyphosate mainly include two methods: glycine method and iminodiacetic acid method.
- the glycine method mainly produces glyphosate by reacting glycine as a raw material. This method has higher yield, higher cost, and consumes a large amount of alkali due to recovery of solvent and catalyst, which increases equipment, energy consumption and workload.
- the iminodiacetic acid method also known as the IDA method, firstly reacts IDA with furfural or phosphorous acid to obtain glyphosate (PMIDA), and then oxidizes PMIDA to obtain glyphosate.
- the raw materials of this method are easy to obtain, simple to operate, the process conditions are moderate, the equipment requirements are not high, the product yield is high, and the economic benefits are good, which is suitable for China's national conditions and domestic market demand. Compared with the one-step method, it has obvious advantages such as low cost.
- the key to PMIDA oxidation is the choice of oxidation process and oxidation catalyst.
- the currently used methods for the oxidative synthesis of glyphosate from glyphosate mainly include two methods of hydrogen peroxide oxidation and catalytic oxidation.
- the hydrogen peroxide oxidation method includes two main ones: one is sodium tungstate-stone ferrous acid as a catalyst or sodium molybdate-sodium metabisulfite as a catalyst, hydrogen peroxide is an oxidant to synthesize glyphosate, and the other is Activated carbon is a catalyst, and hydrogen peroxide is an oxidizing agent for synthesizing glyphosate.
- the first method uses a hydrogen peroxide oxidation method to synthesize glyphosate, which is a long process, including oxidation and reduction.
- the oxidation process has high requirements for the acceleration and temperature of the hydrogen peroxide droplets.
- the catalysts such as ferrous ions or concentrated acid are used in the oxidation process, so that the product is not easy to be placed for a long time, and the yield of the glyphosate raw powder is low, and the product color is yellowish.
- the formation of three wastes of glyphosate mother liquor is an urgent problem to be solved.
- the second method is a method in which activated carbon as reported in the CN1183100 patent is used as a catalyst and oxidized by hydrogen peroxide to prepare glyphosate.
- the advantage of this method is that the catalyst is cheap and easy to obtain, and the process is easy to control.
- the yield of glyphosate raw powder is higher than that of the first process, the cost is less, but the consumption of hydrogen peroxide is twice that of the sodium tungstate-ferrous sulfate-hydrogen peroxide method.
- the activated carbon is easily deactivated and cannot be continuously recycled.
- the preparation of glyphosate by catalytic oxidation utilizes oxygen-containing gas such as air or oxygen as an oxidizing agent, metal or metal salt as a catalyst, and has research value and industrial application value.
- oxygen-containing gas such as air or oxygen
- metal or metal salt as a catalyst
- the catalytic oxidation methods that have been reported are mainly classified into two types: transition metal salt complex catalytic oxidation method and noble metal catalytic oxidation method depending on the type of catalyst.
- Glyphosate is synthesized by catalytic oxidation of diphosphonium with noble metal. The reaction yields high glyphosate content, reaction selectivity and conversion rate. It is reported that Monsanto Company of the United States uses this method to synthesize PMG, which has obvious technical advantages and Economic advantage.
- Monsanto reported a method for preparing glyphosate by using activated carbon supported noble metal as a catalyst, heterogeneous air oxidation, and a method for preparing glyphosate by air oxidation using a noble metal complex containing an organic ligand as a catalyst.
- the defects of these methods include several aspects: 1) Using expensive precious metal catalysts, the catalyst recovery is difficult, and the catalyst is easily lost; 2) The organic ligand preparation method is complicated, which increases the difficulty of product separation and purification. 3) The catalyst needs to be replaced regularly; 4) There are patent restrictions.
- Patent CN96195765.4 reports that activated carbon is a catalyst, first using air as an oxidant, and finally requiring hydrogen peroxide to oxidize the remaining diglycine. Although this method reduces the amount of hydrogen peroxide, it does not completely eliminate the use of hydrogen peroxide. The disadvantage of this method is that the glyphosate needs to react with oxygen or air under a certain pressure to partially react. In view of the deficiencies of the prior art, the inventors conducted in-depth research, and we found in the research that the ultrasonic wave can not only promote the three-phase mixing of the solid-liquid gas, but also continuously update the phase interface, strengthen the mass transfer process, and promote the dissolution of the hg-glyphosate.
- hydroxyl radicals promote the oxidation of activated carbon and oxygen to glyphosate.
- the invention adopts activated carbon and ultrasonic as catalyst, air or oxygen as oxidant, the process is easy to control, the reaction selectivity is high, the amount of by-products is small, the activated carbon is easy to recover, and can be repeatedly applied repeatedly, the reaction liquid is directly concentrated, and the purity of the product can reach 98. %the above. And the product is white, good appearance, high raw powder yield, less mother liquor, low energy consumption, and is the most valuable green new technology in glyphosate synthesis.
- the distinguishing feature of this process is the combination of cheap air and activated carbon and ultrasonic combined oxidation of bisphosphonate, replacing the hydrogen peroxide in the existing method, the expensive precious metal and transition metal, sodium tungstate/sodium molybdate, and no reducing agent.
- the activated carbon used in the present invention includes purified activated carbon prepared by various methods.
- the method combines the advantages of the hydrogen peroxide method and the catalytic oxidation method, on the one hand, overcomes the consumption of a large amount of hydrogen peroxide by the activated carbon-hydrogen peroxide method, directly utilizes air or other oxygen-containing gas as an oxidant, and greatly reduces the cost; on the other hand, the method does not use Activated carbon supported on precious metals can react, overcoming the problems of difficult catalyst recovery, easy loss, and high recovery costs. Therefore, the process has the advantages of low investment, high cost, high quality and no waste.
- An object of the present invention is to provide a process for preparing glyphosate by oxidizing diphosphonate with an oxygen-containing gas in combination with ultrasonic waves and activated carbon.
- the preparation method of the present invention is represented by a synthetic route as follows:
- the main steps of the preparation method of the present invention are:
- the mixed solution of glyphosate (PMIDA), activated carbon and water reacts under ultrasonic wave at a certain temperature, and is detected by nuclear magnetic resonance or liquid chromatography. After the disappearance of the glyphosate, the reaction is stopped, the activated carbon and the product are separated, and the activated carbon is applied. When the activated carbon is used, it can be applied only after simple washing, and has no effect on the reaction selectivity.
- the activated carbon is recovered as a catalyst, and the operation method is the same as above, and the reaction effect is the same.
- the activated carbon prepared by different methods and raw materials was used as a catalyst, and there was no significant difference in reaction selectivity and yield.
- the ultrasonic generator used in this experiment has a frequency of 25 kHz and a power of 100 watts.
- Example 1 The recovered activated carbon in Example 1, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 80 ° C, and the disappearance of the glyphosate was detected, the reaction was stopped, and the reaction time was At 12 hours, the glyphosate reaction selectivity was 90.68%, and finally the glyphosate original powder was 6.53 g, and the content was 99.5%.
- the recovered activated carbon in Example 2 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 90 ° C, and the disappearance of the glyphosate was detected, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 88.4%, and finally the original glyphosate powder was 6.24 g, and the content was 99.4%.
- Example 3 The recovered activated carbon in Example 3, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 70 ° C, and the detection of the disappearance of the glyphosate was stopped, and the reaction was stopped. At 12 hours, the glyphosate reaction selectivity was 91.10%, and finally the glyphosate original powder was 6.55 g, and the content was 99.2%.
- Example 4 The recovered activated carbon in Example 4, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 60 ° C, and the disappearance of the glyphosate was detected, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 90.12%, and finally the original glyphosate powder was 6.50 g, and the content was 99.5%.
- Example 5 The recovered activated carbon in Example 5, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 50 ° C, and the detection of the disappearance of the glyphosate was stopped, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 89.88%, and finally the crude glyphosate powder was 6.48 g, and the content was 99.1%.
- a three-necked flask was charged with 2.5 g of activated carbon (prepared from charcoal), 50 ml of water, 10 g of PMIDA, heated and stirred, and air was introduced into the reaction solution. The temperature was raised to 70 ° C, and the reaction was carried out for 2.5 hours. Phosphorus spectrum detection of glyphosate was carried out. Does not react.
- Comparative Example 3 Add 2.5 g of activated carbon, 50 ml of water, 10 g of PMIDA to the three-necked flask, heat and stir, turn on the ultrasonic generator, and do not pass the gas. The temperature is raised to 70 ° C, and the reaction is carried out for 2.5 hours. Phosphorus is detected without glyphosate formation.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Molecular Biology (AREA)
- Agronomy & Crop Science (AREA)
- Pest Control & Pesticides (AREA)
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Abstract
The invention provides a new preparation method of glyphosate by oxidation of PMIDA, which uses air or oxygen as oxidant and the combination of activated carbon or carbon nanotube with supersonic wave as catalyst. The advantages of the method comprise high yield, high selectivity, high purity of the product, cheap catalyst, low cost, no reducer and no hydrogen peroxide.
Description
一种双甘膦空气氧化制备草甘膦的新工艺 技术领域 A new process for preparing glyphosate by air oxidation of glyphosate
本发明涉及一种双甘膦催化氧化合成重要的农药-除草剂草甘膦 的新工艺。 The invention relates to a novel process for catalytic oxidation of glyphosate to synthesize an important pesticide-herbicide glyphosate.
背景技术 Background technique
草甘膦 (glyphosate, N- (膦羧曱基) -甘氨酸)是美国孟山都化学公司 于 20世纪 60年代筛选合成的一种除草剂, 属于氨基酸衍生物。 草甘 膦良好的生物活性使其成为应用广泛的高效、 低毒、 芽后灭生性除草 剂, 目前年销售额在农药产品中占据首位。 Glyphosate (glyphosate, N-(phosphonocarboxyl)-glycine) is a herbicide selected by Monsanto Chemical Company in the 1960s and belongs to amino acid derivatives. The good biological activity of glyphosate makes it a highly effective, low-toxic, post-emergence herbicide for a wide range of applications. Currently, annual sales rank first among pesticide products.
草甘膦的合成方法主要有甘氨酸法和亚氨基二乙酸法两种。 甘氨 酸法主要以甘氨酸为原料经反应得到草甘膦。 该方法因收率较低, 成 本较高, 并且因回收溶剂和催化剂时要消耗大量碱, 增加了设备、 能 耗和工作量。 亚氨基二乙酸法又称 IDA法, 它先以 IDA与曱醛、 亚磷 酸反应制得双甘膦 (PMIDA),再将 PMIDA氧化得到草甘膦。此法原料 易得、 操作简单、 工艺条件緩和、 对设备要求不高、 产品收率高、 经 济效益好, 适合中国国情及国内市场需求。 与一步法相比, 具有明显 得成本低等方面的优势。 PMIDA氧化的关键是氧化方法和氧化催化剂 的选择。 The synthesis methods of glyphosate mainly include two methods: glycine method and iminodiacetic acid method. The glycine method mainly produces glyphosate by reacting glycine as a raw material. This method has higher yield, higher cost, and consumes a large amount of alkali due to recovery of solvent and catalyst, which increases equipment, energy consumption and workload. The iminodiacetic acid method, also known as the IDA method, firstly reacts IDA with furfural or phosphorous acid to obtain glyphosate (PMIDA), and then oxidizes PMIDA to obtain glyphosate. The raw materials of this method are easy to obtain, simple to operate, the process conditions are moderate, the equipment requirements are not high, the product yield is high, and the economic benefits are good, which is suitable for China's national conditions and domestic market demand. Compared with the one-step method, it has obvious advantages such as low cost. The key to PMIDA oxidation is the choice of oxidation process and oxidation catalyst.
双甘膦氧化合成草甘膦 Oxidative Synthesis of Glyphosate from Glyphos
双甘膦氧化合成草甘膦目前常用的方法主要包括过氧化氢氧化法 和催化氧化法两种。 The currently used methods for the oxidative synthesis of glyphosate from glyphosate mainly include two methods of hydrogen peroxide oxidation and catalytic oxidation.
1、 过氧化氢氧化法
过氧化氢氧化法包括主要两种: 一种是钨酸钠 -石充酸亚铁为催化剂 或者钼酸钠-偏重亚硫酸钠为催化剂, 过氧化氢为氧化剂合成草甘膦的 方法, 另一种是活性炭为催化剂, 过氧化氢为氧化剂合成草甘膦的方 法。 1. Hydrogen peroxide oxidation The hydrogen peroxide oxidation method includes two main ones: one is sodium tungstate-stone ferrous acid as a catalyst or sodium molybdate-sodium metabisulfite as a catalyst, hydrogen peroxide is an oxidant to synthesize glyphosate, and the other is Activated carbon is a catalyst, and hydrogen peroxide is an oxidizing agent for synthesizing glyphosate.
第一种方法采用过氧化氢氧化法合成草甘膦工艺过程较长, 包括 氧化和还原两个过程。 氧化过程对双氧水滴加速度、 温度等控制要求 很高, 同时氧化过程中要采用亚铁离子或者浓酸等催化剂, 使得产品 不易久置, 并且草甘膦原粉收率低, 产品颜色偏黄。 草甘膦母液形成 的三废多, 是目前急需解决的问题。 The first method uses a hydrogen peroxide oxidation method to synthesize glyphosate, which is a long process, including oxidation and reduction. The oxidation process has high requirements for the acceleration and temperature of the hydrogen peroxide droplets. At the same time, the catalysts such as ferrous ions or concentrated acid are used in the oxidation process, so that the product is not easy to be placed for a long time, and the yield of the glyphosate raw powder is low, and the product color is yellowish. The formation of three wastes of glyphosate mother liquor is an urgent problem to be solved.
第二种方法为 CN1183100专利报道的活性炭为催化剂, 双氧水氧 化制备草甘膦的方法, 这种方法的优点在于催化剂廉价易得, 过程容 易控制。 虽然比第一种工艺的草甘膦原粉收率高, 三费少, 但是消耗 的双氧水多,是钨酸钠-硫酸亚铁-双氧水法的消耗量的 2倍。并且活性 炭容易失活, 不能连续回收套用。 The second method is a method in which activated carbon as reported in the CN1183100 patent is used as a catalyst and oxidized by hydrogen peroxide to prepare glyphosate. The advantage of this method is that the catalyst is cheap and easy to obtain, and the process is easy to control. Although the yield of glyphosate raw powder is higher than that of the first process, the cost is less, but the consumption of hydrogen peroxide is twice that of the sodium tungstate-ferrous sulfate-hydrogen peroxide method. Moreover, the activated carbon is easily deactivated and cannot be continuously recycled.
2、 催化氧化法制备草甘膦 2. Preparation of glyphosate by catalytic oxidation
催化氧化法制备草甘膦利用空气或者氧气等含氧气体作为氧化 剂, 金属或金属盐为催化剂, 具有研究价值和工业化应用价值。 已报 道的催化氧化方法根据催化剂种类不同主要分为过渡金属盐络合物催 化氧化法和贵金属催化氧化法两大类。 The preparation of glyphosate by catalytic oxidation utilizes oxygen-containing gas such as air or oxygen as an oxidizing agent, metal or metal salt as a catalyst, and has research value and industrial application value. The catalytic oxidation methods that have been reported are mainly classified into two types: transition metal salt complex catalytic oxidation method and noble metal catalytic oxidation method depending on the type of catalyst.
1、 过渡金属络合物催化氧化法和贵金属催化剂催化氧化法 1. Catalytic oxidation of transition metal complexes and catalytic oxidation of noble metal catalysts
孟山都公司对此进行了较多研究, 过渡金属如锰、 钴、 钒等盐的络 合物,在氧气存在下可以催化氧化双甘膦生成草甘膦,专利 (EP0314662) 推荐的氧化温度为 70 ~ 100°C, 压力为 30-1000psig, 氧气采用鼓泡方 式通入双甘膦水溶液中。 和贵金属催化剂相比, 过渡金属催化剂成本 低廉, 属于均相催化, 省去了工艺过程中催化剂过滤工段, 简化了工
过渡金属虽然成本低廉, 但目标产品转化率和催化剂选择性不如 贵金属催化剂, 且反应条件相对较为苛刻。 采用贵金属催化氧化双甘 膦的方法合成草甘膦, 反应得到的草甘膦含量高, 反应的选择性和转 化率也都很好据悉美国孟山都公司就是采用此法合成 PMG,具有明显 技术优势和经济优势。 Monsanto has conducted more research on this. Complexes of transition metals such as manganese, cobalt and vanadium can catalyze the oxidation of glyphosate in the presence of oxygen. The patent (EP0314662) recommends an oxidation temperature of 70. ~ 100 ° C, pressure 30-1000 psig, oxygen is bubbled into the aqueous solution of diglycine. Compared with precious metal catalysts, transition metal catalysts are low in cost and belong to homogeneous catalysis, eliminating the catalyst filtration section in the process and simplifying the work. Although the transition metal is low in cost, the target product conversion rate and catalyst selectivity are not as good as those of the precious metal catalyst, and the reaction conditions are relatively harsh. Glyphosate is synthesized by catalytic oxidation of diphosphonium with noble metal. The reaction yields high glyphosate content, reaction selectivity and conversion rate. It is reported that Monsanto Company of the United States uses this method to synthesize PMG, which has obvious technical advantages and Economic advantage.
文献 (US3950402)介绍用贵金属 (Pd、 Pt、 Rh等)负载在活性炭上, 通入氧气氧化双甘膦, 在温度 90°C ~ 100°C, 压力 30psig下, 反应 3h 可以得到纯度 97%的草甘膦, 产率可达 96%。 The literature (US3950402) introduces the use of precious metals (Pd, Pt, Rh, etc.) supported on activated carbon, and oxidizes glyphosate with oxygen. At a temperature of 90 ° C to 100 ° C and a pressure of 30 psig, a purity of 97% can be obtained by reacting for 3 hours. Glyphosate, yield up to 96%.
孟山度报道了活性炭负载贵金属做催化剂,非均相空气氧化制备草 甘膦的方法; 以及含有机配体的贵金属配合物做催化剂, 空气氧化制 备草甘膦的方法。 这些方法的缺陷包括几个方面: 1 )使用昂贵的贵金 属催化剂, 催化剂回收困难, 催化剂极易流失; 2 )有机配体制备方法 复杂, 增加了产品分离纯化难度。 3 )催化剂需要定期更换; 4 )存在 专利限制。 Monsanto reported a method for preparing glyphosate by using activated carbon supported noble metal as a catalyst, heterogeneous air oxidation, and a method for preparing glyphosate by air oxidation using a noble metal complex containing an organic ligand as a catalyst. The defects of these methods include several aspects: 1) Using expensive precious metal catalysts, the catalyst recovery is difficult, and the catalyst is easily lost; 2) The organic ligand preparation method is complicated, which increases the difficulty of product separation and purification. 3) The catalyst needs to be replaced regularly; 4) There are patent restrictions.
3、 活性炭 -空气 -双氧水催化氧化法 3, activated carbon - air - hydrogen peroxide catalytic oxidation
专利 CN96195765.4报道了活性炭为催化剂, 先利用空气作为氧化 剂, 最后还需要双氧水氧化剩余的双甘膦。 虽然此方法减少了双氧水 的用量, 但是没有根本消除双氧水的使用。 该方法的不足之处是双甘 膦需要在一定压力下和氧气或者空气反应才能部分反应。 针对现有技术的不足, 本发明者进行了深入的研究, 我们在研究 中发现, 超声波不但能促进固液气三相混合, 能不断更新相界面, 强 化传质过程, 促进汉甘膦的溶解和分散, 而且可以在溶液中产生羟基 自由基, 羟基自由基促进活性炭和氧气对双甘膦的氧化作用。
本发明以活性炭和超声波为催化剂, 空气或者氧气为氧化剂, 过 程容易控制, 反应选择性高, 副产物量少, 活性炭易回收, 并且可多 次反复套用, 反应液直接浓缩, 产品纯度可达到 98%以上。 并且产品 为白色, 外观好, 原粉收率高, 母液少, 物耗能耗低, 是草甘膦合成 中最有价值的绿色新工艺。 本工艺的显著特点是用廉价的空气和活性 炭以及超声波组合氧化双甘膦, 代替了现有方法中的双氧水, 吊贵的 贵金属和过渡金属、 钨酸钠 /钼酸钠, 而且不使用还原剂。 本发明中使 用的活性炭包括用各种方法制备的、 纯化处理的活性炭。 本方法综合 了过氧化氢法和催化氧化法的优点, 一方面克服了活性炭 -双氧水法消 耗大量双氧水, 直接利用了空气或其它含氧气体为氧化剂, 大大减少 成本; 另一方面本方法不使用贵金属负载的活性炭就可反应, 克服了 催化剂难回收、 容易流失, 回收成本高等问题。 因此该工艺具有投资 少, 成本^ ί氏, 品质高, 无三废的优点。 Patent CN96195765.4 reports that activated carbon is a catalyst, first using air as an oxidant, and finally requiring hydrogen peroxide to oxidize the remaining diglycine. Although this method reduces the amount of hydrogen peroxide, it does not completely eliminate the use of hydrogen peroxide. The disadvantage of this method is that the glyphosate needs to react with oxygen or air under a certain pressure to partially react. In view of the deficiencies of the prior art, the inventors conducted in-depth research, and we found in the research that the ultrasonic wave can not only promote the three-phase mixing of the solid-liquid gas, but also continuously update the phase interface, strengthen the mass transfer process, and promote the dissolution of the hg-glyphosate. And dispersion, and can generate hydroxyl radicals in solution, hydroxyl radicals promote the oxidation of activated carbon and oxygen to glyphosate. The invention adopts activated carbon and ultrasonic as catalyst, air or oxygen as oxidant, the process is easy to control, the reaction selectivity is high, the amount of by-products is small, the activated carbon is easy to recover, and can be repeatedly applied repeatedly, the reaction liquid is directly concentrated, and the purity of the product can reach 98. %the above. And the product is white, good appearance, high raw powder yield, less mother liquor, low energy consumption, and is the most valuable green new technology in glyphosate synthesis. The distinguishing feature of this process is the combination of cheap air and activated carbon and ultrasonic combined oxidation of bisphosphonate, replacing the hydrogen peroxide in the existing method, the expensive precious metal and transition metal, sodium tungstate/sodium molybdate, and no reducing agent. . The activated carbon used in the present invention includes purified activated carbon prepared by various methods. The method combines the advantages of the hydrogen peroxide method and the catalytic oxidation method, on the one hand, overcomes the consumption of a large amount of hydrogen peroxide by the activated carbon-hydrogen peroxide method, directly utilizes air or other oxygen-containing gas as an oxidant, and greatly reduces the cost; on the other hand, the method does not use Activated carbon supported on precious metals can react, overcoming the problems of difficult catalyst recovery, easy loss, and high recovery costs. Therefore, the process has the advantages of low investment, high cost, high quality and no waste.
发明内容 Summary of the invention
本发明的目的是提供一种以超声波和活性炭联合作用下, 含氧气 体氧化双甘膦制备草甘膦的方法。 SUMMARY OF THE INVENTION An object of the present invention is to provide a process for preparing glyphosate by oxidizing diphosphonate with an oxygen-containing gas in combination with ultrasonic waves and activated carbon.
本发明的制备方法用合成路线表示如下:
The preparation method of the present invention is represented by a synthetic route as follows:
具体的说, 本发明的制备方法其主要步骤是: Specifically, the main steps of the preparation method of the present invention are:
双甘膦 (PMIDA)、 活性炭和水的混合溶液在一定温度下在超声波 作用下反应, 用核磁共振或液相色语检测, 双甘膦消失后停止反应, 分离出活性炭和产品, 活性炭套用。 活性炭套用时只需对其进行简单 洗涤后即可套用, 对反应选择性无影响。
回收活性炭作为催化剂, 操作方法同上, 反应效果相同。 不同方法 和原料制备的活性炭做催化剂, 反应选择性和收率无显著差别。 The mixed solution of glyphosate (PMIDA), activated carbon and water reacts under ultrasonic wave at a certain temperature, and is detected by nuclear magnetic resonance or liquid chromatography. After the disappearance of the glyphosate, the reaction is stopped, the activated carbon and the product are separated, and the activated carbon is applied. When the activated carbon is used, it can be applied only after simple washing, and has no effect on the reaction selectivity. The activated carbon is recovered as a catalyst, and the operation method is the same as above, and the reaction effect is the same. The activated carbon prepared by different methods and raw materials was used as a catalyst, and there was no significant difference in reaction selectivity and yield.
具体实施方式 Detailed ways
实施例 1 Example 1
本实验所使用的超声波发生器频率为 25KHz, 功率为 100W。 The ultrasonic generator used in this experiment has a frequency of 25 kHz and a power of 100 watts.
三口烧瓶中加入 2.5克活性炭 (木炭为原料制备的), 50毫升水, 10 克 PMIDA, 加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温 度升至 40°C , 检测至双甘膦完全反应, 反应时间 15 小时, 草甘膦反 应选择性 89.1%, 最后得到草甘膦原粉 6.49g, 含量 99%。 Add 2.5 g of activated carbon (made of charcoal as raw material) to a three-necked flask, 50 ml of water, 10 g of PMIDA, heat and stir, introduce air into the reaction solution, turn on the ultrasonic generator, and raise the temperature to 40 ° C to detect the glyphosate. Complete reaction, reaction time 15 hours, glyphosate reaction selectivity 89.1%, finally obtained glyphosate original powder 6.49g, content 99%.
实施例 2: Example 2:
实施例 1中的回收活性炭, 100毫升水, 10克 PMIDA,加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温度升至 80°C , 检测至双 甘膦消失, 反应停止, 反应时间 12小时, 草甘膦反应选择性 90.68%, 最后得到草甘膦原粉 6.53g, 含量 99.5%。 The recovered activated carbon in Example 1, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 80 ° C, and the disappearance of the glyphosate was detected, the reaction was stopped, and the reaction time was At 12 hours, the glyphosate reaction selectivity was 90.68%, and finally the glyphosate original powder was 6.53 g, and the content was 99.5%.
实施例 3: Example 3:
实施例 2中的回收活性炭, 100毫升水, 10克 PMIDA,加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温度升至 90°C, 检测至双 甘膦消失, 反应停止, 反应时间 12小时, 草甘膦反应选择性 88.4%, 最后得到草甘膦原粉 6.24g, 含量 99.4%。 The recovered activated carbon in Example 2, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 90 ° C, and the disappearance of the glyphosate was detected, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 88.4%, and finally the original glyphosate powder was 6.24 g, and the content was 99.4%.
实施例 4: Example 4:
实施例 3中的回收活性炭, 100毫升水, 10克 PMIDA,加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温度升至 70°C , 检测至双 甘膦消失, 反应停止, 反应时间 12小时, 草甘膦反应选择性 91.10%, 最后得到草甘膦原粉 6.55g, 含量 99.2%。
实施例 4中的回收活性炭, 100毫升水, 10克 PMIDA,加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温度升至 60°C , 检测至双 甘膦消失, 反应停止, 反应时间 12小时, 草甘膦反应选择性 90.12%, 最后得到草甘膦原粉 6.50g, 含量 99.5%。 The recovered activated carbon in Example 3, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 70 ° C, and the detection of the disappearance of the glyphosate was stopped, and the reaction was stopped. At 12 hours, the glyphosate reaction selectivity was 91.10%, and finally the glyphosate original powder was 6.55 g, and the content was 99.2%. The recovered activated carbon in Example 4, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 60 ° C, and the disappearance of the glyphosate was detected, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 90.12%, and finally the original glyphosate powder was 6.50 g, and the content was 99.5%.
实施例 6: Example 6:
实施例 5中的回收活性炭, 100毫升水, 10克 PMIDA,加热搅拌, 向反应溶液通入空气, 开启超声波发生器, 温度升至 50°C , 检测至双 甘膦消失, 反应停止, 反应时间 12小时, 草甘膦反应选择性 89.88%, 最后得到草甘膦原粉 6.48g, 含量 99.1%。 The recovered activated carbon in Example 5, 100 ml of water, 10 g of PMIDA, heated and stirred, air was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 50 ° C, and the detection of the disappearance of the glyphosate was stopped, and the reaction was stopped. At 12 hours, the selectivity of glyphosate reaction was 89.88%, and finally the crude glyphosate powder was 6.48 g, and the content was 99.1%.
上述 6批反应分离活性炭后得溶液集中处理, 分离出草甘膦原粉 的含量均大于 98%, 收率大于 87%。 After the above six batches of reaction were separated and activated carbon, the solution was concentrated, and the content of the original glyphosate powder was more than 98%, and the yield was more than 87%.
实施例 7: Example 7
三口烧瓶中加入 2.5克活性炭, 50毫升水, 10克 PMIDA, 加热搅 拌, 由水泵吸空气通入反应溶液, 开启超声波发生器, 温度升至 78°C , 磷镨检测至双甘膦完全反应, 反应约 16 小时, 草甘膦反应选择性 90.1%, 最后得到草甘膦原粉 6.44g, 含量 98.5%。 Add 2.5 g of activated carbon, 50 ml of water, 10 g of PMIDA to the three-necked flask, heat and stir. The air is sucked into the reaction solution by the pump, the ultrasonic generator is turned on, the temperature is raised to 78 ° C, and the phosphonium is detected to completely react with the glyphosate. The reaction was about 16 hours, and the selectivity of glyphosate reaction was 90.1%. Finally, the original glyphosate powder was 6.44 g, and the content was 98.5%.
实施例 8: Example 8
三口烧瓶中加入 2.5克活性炭, 50毫升水, 10克 P DA, 加热搅 拌, 常压下氧气通入反应溶液, 开启超声波发生器, 温度升至 63 °C , 磷谱检测至双甘膦完全反应,反应约 3小时,草甘膦反应选择性 89.1%, 最后得到草甘膦原粉 6.40g, 含量 98.2%。 Add 2.5 g of activated carbon, 50 ml of water, 10 g of P DA to the three-necked flask, heat and stir. Oxygen is introduced into the reaction solution under normal pressure, the ultrasonic generator is turned on, the temperature is raised to 63 ° C, and the phosphorus spectrum is detected to completely react with the glyphosate. The reaction was about 3 hours, and the selectivity of glyphosate reaction was 89.1%. Finally, the original glyphosate powder was 6.40 g, and the content was 98.2%.
实施例 9: Example 9
高压釜中加入 2.5克活性炭, 50毫升水, 10克 PMIDA,加热搅拌, 将空气通入反应溶液, 开启超声波发生器, 温度升至 50 °C , 压力 0.5MPa, 磷谱检测至双甘膦完全反应, 反应约 2小时, 草甘膦反应选
择性 88.1%, 最后得到草甘膦原粉 6.39g, 含量 98.2%。 Add 2.5 g of activated carbon, 50 ml of water, 10 g of PMIDA to the autoclave, heat and stir, pass air into the reaction solution, turn on the ultrasonic generator, the temperature is raised to 50 °C, the pressure is 0.5 MPa, and the phosphorus spectrum is detected to be completely glyphosate. Reaction, reaction for about 2 hours, glyphosate reaction selection Selective 88.1%, the final glyphosate powder 6.39g, the content of 98.2%.
实施例 10: Example 10
三口瓶中加入 5.0克活性炭, 50毫升水, 10克 PMIDA,加热搅拌, 将空气通入反应溶液, 开启超声波发生器, 温度升至 55°C , 磷语检测 至双甘膦完全反应, 反应约 6小时, 草甘膦反应选择性 87.1%, 最后 得到草甘膦原粉 6.35g, 含量 98.3%。 Add 5.0 g of activated carbon, 50 ml of water, 10 g of PMIDA to the three-necked bottle, heat and stir, pass air into the reaction solution, turn on the ultrasonic generator, and the temperature rises to 55 ° C. The phosphorus is detected to completely react with the glyphosate. At 6 hours, the glyphosate reaction selectivity was 87.1%, and finally the glyphosate original powder was 6.35 g, and the content was 98.3%.
实施例 11 : Example 11:
三口瓶中加入 4.0克活性炭, 50毫升水, 10克 PMIDA,加热搅拌, 将空气通入反应溶液, 开启超声波发生器, 温度升至 65°C , 磷语检测 至双甘膦完全反应, 反应约 8小时, 草甘膦反应选择性 86.6%, 最后 得到草甘膦原粉 6.32g, 含量 98.0%。 Add 4.0 g of activated carbon, 50 ml of water, 10 g of PMIDA to the three-necked bottle, heat and stir, pass the air into the reaction solution, turn on the ultrasonic generator, and the temperature rises to 65 ° C. The phosphorus is detected to completely react with the glyphosate. At 8 hours, the glyphosate reaction selectivity was 86.6%, and finally the glyphosate original powder was 6.32 g, and the content was 98.0%.
实施例 12: Example 12:
三口瓶中加入 2.5克活性炭, 150毫升水, 10克 PMIDA, 加热搅 拌, 将氧气通入反应溶液, 开启超声波发生器, 温度升至 65°C , 磷谱 检测至双甘膦完全反应, 反应约 10小时, 草甘膦反应选择性 87.4%, 最后得到草甘膦原粉 6.30g, 含量 98.5%。 Add 2.5 g of activated carbon, 150 ml of water, 10 g of PMIDA to the three-necked bottle, heat and stir, pass oxygen into the reaction solution, turn on the ultrasonic generator, the temperature rises to 65 ° C, and the phosphorus spectrum is detected to completely react with the glyphosate. At 10 hours, the glyphosate reaction selectivity was 87.4%, and finally the glyphosate original powder was 6.30 g, and the content was 98.5%.
实施例 13: Example 13
三口瓶中加入 2.0克活性炭, 250毫升水, 10克 PMIDA, 加热搅 拌, 将氧气通入反应溶液, 开启超声波发生器, 温度升至 65°C , 磷谱 检测至双甘膦完全反应, 反应约 8小时, 草甘膦反应选择性 88.2%, 最后得到草甘膦原粉 6.38g, 含量 98.4%。 Add 2.0 g of activated carbon, 250 ml of water, 10 g of PMIDA to the three-necked bottle, heat and stir, pass oxygen into the reaction solution, turn on the ultrasonic generator, the temperature rises to 65 ° C, and the phosphorus spectrum is detected to completely react with the glyphosate. At 8 hours, the glyphosate reaction selectivity was 88.2%, and finally the glyphosate original powder was 6.38 g, and the content was 98.4%.
实施例 14: Example 14
三口瓶中加入 2.5克碳纳米管, 100毫升水, 10克 PMIDA, 加热 搅拌, 将氧气通入反应溶液, 开启超声波发生器, 温度升至 65°C , 磷 谱检测至双甘膦完全反应,反应约 15小时,草甘膦反应选择性 85.9%,
最后得到草甘膦原粉 6.17g, 含量 98.1%。 2.5 grams of carbon nanotubes, 100 ml of water, 10 g of PMIDA were added to the three-necked flask, heated and stirred, oxygen was introduced into the reaction solution, the ultrasonic generator was turned on, the temperature was raised to 65 ° C, and the phosphorus spectrum was detected to completely react with the glyphosate. The reaction is about 15 hours, and the selectivity of glyphosate reaction is 85.9%. Finally, 6.17 g of glyphosate powder was obtained, and the content was 98.1%.
实施例 15: Example 15
5克碳纳米管 (Fe-Mo/A1203制备的典型多壁碳纳米管)与约 100毫 升浓硝酸混合, 加热至 90摄氏度, 持续搅拌 3 ~ 4小时。 过滤, 滤渣 碳纳米管用去离子水洗至中性。 Five grams of carbon nanotubes (typical multi-walled carbon nanotubes prepared by Fe-Mo/A1203) were mixed with about 100 milliliters of concentrated nitric acid, heated to 90 degrees Celsius, and stirred continuously for 3-4 hours. Filtration, filter residue Carbon nanotubes were washed with deionized water to neutrality.
三口瓶中加入 2.5 克经过硝酸处理的碳纳米管, 100 毫升水, 10 克 PMIDA, 加热搅拌, 将氧气通入反应溶液, 开启超声波发生器, 温 度升至 65°C, 磷语检测至双甘膦完全反应, 反应约 10小时, 草甘膦 反应选择性 87.9%, 最后得到草甘膦原粉 6.30g, 含量 98.4%。 Add 2.5 grams of nitric acid treated carbon nanotubes, 100 ml of water, 10 g of PMIDA to the three-necked flask, heat and stir, pass oxygen to the reaction solution, turn on the ultrasonic generator, and raise the temperature to 65 ° C. The phosphine was completely reacted, the reaction was about 10 hours, the glyphosate reaction selectivity was 87.9%, and finally the glyphosate original powder was 6.30 g, and the content was 98.4%.
下示为发明者使用的碳纳米管的一些基本参数 Some basic parameters of the carbon nanotubes used by the inventors are shown below.
Fe-Mo/A1203制备的典型多壁碳纳米管 Typical multi-walled carbon nanotubes prepared by Fe-Mo/A1203
外管径: 8.6nm Outer diameter: 8.6nm
内管径: 3.5nm Inner diameter: 3.5nm
堆比重: 0.05g/cm3 Heap specific gravity: 0.05g/cm3
比表面积: 200-300m2/g Specific surface area: 200-300m2/g
含碳量: 98% Carbon content: 98%
对比实施例 1 Comparative Example 1
三口烧瓶中加入 2.5克活性炭 (木炭为原料制备的), 50毫升水, 10 克 PMIDA, 加热搅拌, 向反应溶液通入空气, 温度升至 70°C , 反应 2.5小时, 磷谱检测双甘膦不反应。 A three-necked flask was charged with 2.5 g of activated carbon (prepared from charcoal), 50 ml of water, 10 g of PMIDA, heated and stirred, and air was introduced into the reaction solution. The temperature was raised to 70 ° C, and the reaction was carried out for 2.5 hours. Phosphorus spectrum detection of glyphosate was carried out. Does not react.
对比实施例 2 Comparative Example 2
三口烧瓶中加入 50毫升水, 10克 PMIDA, 加热搅拌, 向反应溶 液通入空气, 开启超声波发生器, 温度升至 70°C, 反应 2.5小时, 磷 语检测没有草甘膦生成。 50 ml of water, 10 g of PMIDA was added to the three-necked flask, and the mixture was heated and stirred. Air was introduced into the reaction solution, and the ultrasonic generator was turned on. The temperature was raised to 70 ° C for 2.5 hours, and no phosphorus glyphosate was formed in the phosphorus detection.
对比实施例 3
三口烧瓶中加入 2.5克活性炭, 50毫升水, 10克 PMIDA, 加热搅 拌, 开启超声波发生器, 不通入气体, 温度升至 70°C, 反应 2.5小时, 磷傅检测没有草甘膦生成。 Comparative Example 3 Add 2.5 g of activated carbon, 50 ml of water, 10 g of PMIDA to the three-necked flask, heat and stir, turn on the ultrasonic generator, and do not pass the gas. The temperature is raised to 70 ° C, and the reaction is carried out for 2.5 hours. Phosphorus is detected without glyphosate formation.
对比实施例 4 Comparative Example 4
三口烧瓶中加入钨酸钠 0.06克, 50毫升水, 20克 PMIDA, 加热 搅拌, 温度升至 60°C , 滴加 5.6克 30%双氧水, 保温反应 1小时, 磷 语检测几乎没有双甘膦, 降温, 滴加硫酸亚铁溶液, 最终草甘膦转化 率 90%, 原粉收率 72.5%。
Add 0.06 g of sodium tungstate, 50 ml of water, 20 g of PMIDA to the three-necked flask, heat and stir, the temperature is raised to 60 ° C, 5.6 g of 30% hydrogen peroxide is added dropwise, and the reaction is kept for 1 hour. The phosphorus detection has almost no glyphosate. The temperature was lowered, and the ferrous sulfate solution was added dropwise. The final conversion rate of glyphosate was 90%, and the original powder yield was 72.5%.
Claims
1、 一种以超声波和活性炭或碳纳米管联合催化作用, 用空气或者 氧气直接氧化双甘膦制备草甘膦的新工艺。 1. A new process for the preparation of glyphosate by direct oxidation of glyphosate with air or oxygen by the combined action of ultrasonic waves and activated carbon or carbon nanotubes.
2、 根据权利要求 1所述的方法, 其中, 超声波为任何能引发超声 波的设备, 超声波通过固液介盾传递到反应体系的机械波, 其一般频 率大于 15KHz。 2. The method according to claim 1, wherein the ultrasonic wave is any device capable of inducing ultrasonic waves, and the ultrasonic wave is transmitted to the mechanical wave of the reaction system through the solid-liquid shield, and the general frequency is greater than 15 kHz.
3、 根据权利要求 1所述的方法, 其中, 活性炭为任何来源的活性 炭或多孔含碳物质, 活性炭与碳纳米管或无机物的混合物, 负载金属 或贵金属的活性炭, 回收套用的活性炭。 The method according to claim 1, wherein the activated carbon is activated carbon or porous carbonaceous material of any source, a mixture of activated carbon and carbon nanotubes or inorganic materials, activated carbon loaded with metal or precious metal, and recycled activated carbon.
4、 根据权利要求 1所述的方法, 其中, 碳纳米管包括用各种方法 制备的多壁、单壁或混合体碳纳米管, 也可以是回收套用的碳纳米管。 优选表面经过处理、 含羟基和 /或羧基较多的碳纳米管。 4. The method according to claim 1, wherein the carbon nanotubes comprise multi-walled, single-walled or mixed carbon nanotubes prepared by various methods, and may also be carbon nanotubes for recycling. Preferred are carbon nanotubes having a surface treated with a large amount of hydroxyl groups and/or carboxyl groups.
5、 根据权利要求 1 所述的方法, 其中, 活性炭 /碳纳米管的用量 为双甘膦重量的 0.05%-100%重量, 优选 5%-50%。 The method according to claim 1, wherein the activated carbon/carbon nanotube is used in an amount of 0.05% by weight to 100% by weight, preferably 5% to 50% by weight based on the weight of the glyphosate.
6、 根据权利要求 1所述的方法, 其中, 反应温度为 20- 100 °C , 优 选 40-80°C。 The method according to claim 1, wherein the reaction temperature is 20 to 100 ° C, preferably 40 to 80 ° C.
7、 根据权利要求 1 所述的方法, 其中, 含氧气体为空气和 /或氧 气和 /或其它含氧气体, 优选空气。 7. A method according to claim 1 wherein the oxygen containing gas is air and / or oxygen and / or other oxygen containing gas, preferably air.
8、 根据权利要求 1所述的方法, 其中, 反应压力可以在常压、 减 压、 工业反应器能够耐受的压力下。 8. The method of claim 1 wherein the reaction pressure is at atmospheric pressure, reduced pressure, and pressure that the industrial reactor can withstand.
9、 根据权利要求 1所述的方法, 其中, 反应体系加水量为双甘膦 重量的 1-50倍, 优选 2-30倍。 The method according to claim 1, wherein the reaction system is added in an amount of from 1 to 50 times, preferably from 2 to 30 times the weight of the glyphosate.
10、 根据权利要求 1所述的方法, 其中, 反应器为工业上采用的 各种形式的反应器, 如内置超声发生器的釜式反应器、 具有循环特征
的外置式超声发生器的管式反应器、 具有循环特征的外置式超声反应 器。 10. The method according to claim 1, wherein the reactor is various types of reactors industrially employed, such as a tank reactor with an ultrasonic generator built therein, having a cycle characteristic A tubular reactor of an external ultrasonic generator, an external ultrasonic reactor having a circulating characteristic.
11、 根据权利要求 1所述的方法, 其中, 反应方式为连续或者间 歇式反应。 11. The method according to claim 1, wherein the reaction mode is a continuous or intermittent reaction.
12、 根据权利要求 1所述的方法, 其中, 可以是活性炭和碳纳米 管的混合物。
12. The method of claim 1 wherein it may be a mixture of activated carbon and carbon nanotubes.
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