Method and device for producing N-phosphono methyl glycine
A technology of phosphonomethylglycine and production method, applied in the field of N-phosphonomethyliminodiacetic acid, can solve the problems of affecting the productivity of equipment, blockage of fixed bed, poor heat transfer effect of fixed bed and the like
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Embodiment 1
[0062] Under the temperature of 100~110 ℃ and the pressure of 0.1~0.5MPa, put 98% PMIDA and deionized water into the feed mixer according to a certain proportion and be mixed with the aqueous solution of 3% bisglyphosate in concentration by weight, Squeeze into the tubular reactor that 3Kg gac catalyst is housed after metering with pump then. Pure oxygen gas was metered into the tubular reactor at a rate of 7.3 g / min. The reactor pressure was maintained at about 0.3 MPa. Experiments were performed at various temperatures and liquid feed rates. The reaction results are shown in Table 1.
[0063] Table 1
[0064]
Embodiment 2
[0066] Example 2-1, Step 1: Repeat the operation in Example 1, other operating conditions remain unchanged, inject the diglyphosate aqueous solution into the tubular reactor at a liquid feed rate of 430 g / min. The reaction temperature was maintained at about 110°C. Step 2: The obtained glyphosate feed liquid is discharged and concentrated in the concentration tank. The processed feed liquid is fully crystallized, filtered and separated, and the filtrate is the glyphosate mother liquid, weighing 184Kg. After recovery, it is recycled to the concentration section, wet After drying the powder, glyphosate crystals were obtained, weighing 16Kg, with a measured content of 97.5% and a yield of 85%.
[0067] Example 2-2, repeat the operation in Example 2-1, after the glyphosate feed liquid obtained in step 2 is discharged into the concentration tank, add the glyphosate mother liquor obtained in Example 2-1 together to concentrate in the concentration tank , the treated feed liquid is ...
Embodiment 3
[0070] Under the temperature of 120~140 ℃ and the pressure of 0.2~0.4MPa, put 98% PMIDA and deionized water into the feed mixer according to a certain proportion and be mixed with the aqueous solution of 6% diglyphosate in weight percent concentration, Then push into the tubular reactor that 4.5Kg activated carbon catalyst is housed after metering with a pump. Pure oxygen gas was metered into the tubular reactor at a rate of 6.4 g / min. The reactor pressure was maintained at about 0.5 MPa. Experiments were performed at various temperatures and liquid feed rates. The reaction results are shown in Table 2.
[0071] Table 2
[0072]
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