Method for producing N-alkyl substituted phosphoric triamide

A technology for the production of phosphoric triamides, applied in chemical instruments and methods, phosphate fertilizers, organic phosphate fertilizers, etc., can solve the problems of unfavorable purification of final products, high requirements for production conditions, cumbersome operation steps, etc., and achieve simple solvent recovery process, The product purity and yield are improved, and the process is simple

Inactive Publication Date: 2009-01-07
张九治
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

At present, there are few bibliographical reports on the production method of N-n-butylthiophosphoric triamide. Existing patents US5770771, US5883297 and DE102005053541 involve low-temperature reactions in the reported production process, or require a certain degree of vacuum, or The reaction that requires a certain pressure requires high production conditions. Triethylamine is used as an acid-binding agent in the production process, which increases the difficulty of separation. In addition, the amount of ammonia used is large, resulting in a certain degree of waste of resources. It needs to be used in the final post-processing Only special equipment can get the product, and the operation steps are cumbersome
The production method of N-n-butylthiophosphoric triamide reported in domestic patent literature [publication number CN1583767] also involves low-temperature reaction, and triethylamine is also used to absorb the hydrochloric acid produced in the production, which is unfavorable for the purification of the final product

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  • Method for producing N-alkyl substituted phosphoric triamide

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Embodiment 1

[0016] The production process in the No. 1 reactor:

[0017] The No. 1 reactor is a mechanically stirred tank, and the stirring speed of the No. 1 reactor is controlled at 20rpm to 60rpm. The heat exchange device used is a reflux cooling device, and the cooling medium is water, ice water or calcium chloride freezing liquid.

[0018] In Reactor No. 1, mix and match 1L to 1.6L of solvent according to 1 mole of chlorine phosphorus solution, and add 50Kg of PSCl 3 , 384Kg of CH 2 Cl 2 , mixed and stirred at a speed of 30rpm until the temperature was cooled to 5-15°C, and the alkylamine was added dropwise.

[0019] According to the molar ratio range of chlorophosphorus solution to alkylamine in the range of 1:1.95 to 1:2.1, 43.3Kg of n-butylamine is dropped into the cooled feed liquid, and excess n-butylamine is used as an acid-binding agent. Control the rate of addition to keep the temperature of the reaction system at 10-12°C. After the dropwise addition is completed, the rea...

Embodiment 2

[0031] The production process in the No. 1 reactor:

[0032] This No. 1 reaction kettle is a magnetic stirring tank, and the heat exchange device used is a reflux cooling device, and the cooling medium therein is water, and ice water can also use calcium chloride freezing liquid.

[0033] Add 50Kg of PSCl in No. 1 reactor 3 , 384Kg CH 2 Cl 2 , stirred and cooled to 10°C, added dropwise 45.3Kg of n-hexylamine, and controlled the rate of addition to keep the temperature of the reaction system at 10-15°C. After the dropwise addition was completed, the reaction system was heated under normal pressure to reflux state, refluxed for 1 hour, cooled, added 50 L of water and stirred at 20 rpm for 15 minutes, left to separate for about 2 hours, and the aqueous phase and the organic phase were separated.

[0034] The organic phase was dried over anhydrous sodium sulfate and put into No. 2 reaction kettle for later use.

[0035] The production process in the No. 2 reactor:

[0036] Un...

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Abstract

The invention provides a method for producing N-alkyl substitution phosphoryl triamide, which comprises the following steps: phosphorus chloride liquid is mixed with at least one organic solvent for precooling, then alkylamine solution is added drop by drop, and the reaction temperature ranging from 10 to 12 DEG C is kept; refluxing through heating is performed after adding drop by drop until the reaction is completed; after the reaction feed solution is washed and an organic layer is dried through dryer, ammonia gas is pumped in the next reaction; the pumping speed of ammonia gas is controlled, and the temperature of a reaction system is kept within 10 to 30 DEG C until the reaction is completed; generated solid in the reaction system is separated; the obtained organic layer is distilled to remove most solvent after being washed and separated; residue is a crude product that is N-alkyl substitution phosphoryl triamide containing a formula (1), and the crude product is recrystallized so as to obtain a fine product, the purity quotient of which is more than 98 percent. Compared with other prior arts, the method has the characteristics that the reaction condition is mild, the technology is simple, the cost is low, the purity quotient of the product is high, etc., and the method is particularly suitable for industrialized production.

Description

technical field [0001] The invention relates to a preparation method of N-alkyl substituted phosphoric triamide, in particular to a production method of N-alkyl substituted phosphoric triamide. Background technique [0002] N-Alkyl-substituted phosphoric triamides are highly effective urokinase inhibitors. At present, urea, which is the most widely used in the world, must be converted into ammonium carbamate through the enzymatic hydrolysis of urokinase in the soil, and absorbed by plants in the form of ammonium nitrogen. Due to the high activity of urokinase in the soil, the rate of converting urea to release ammonium nitrogen is very fast, and before the crops can absorb it, they will be volatilized and lost as ammonia nitrogen. Some of the ammonium nitrogen that is not absorbed by crops can also be converted into nitrate nitrogen, which will cause the deterioration of the atmosphere and soil environment through leaching and volatilization. N-alkyl substituted phosphoric...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F9/22C05B15/00
Inventor 张九治
Owner 张九治
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