Alkyl ester method glyphosate solvent recovery system and process

A recovery system and glyphosate technology, applied in the chemical industry, separation methods, chemical instruments and methods, etc., can solve the problems of poor intrinsic safety, low energy consumption of phase transition, poor operation stability, etc., to avoid large logistics load, Improves intrinsic safety and reduces system stress

Pending Publication Date: 2018-08-10
HUBEI TAISHENG CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] This method is easy to operate but has the disadvantages of being highly dependent on graphite condensers, poor in intrinsic safety and high energy consumption: the hydrolysis tail gas of this process is acidic gas containing a large amount of hydrogen chloride, so it is highly dependent on graphite condensers
[0010] This method has less phase change and low energy consumption, but has the disadvantages of poor operation stability: First, the remaining tail gas after hydrolyzing the tail gas to remove hydrogen chloride gas is composed of methylal (A)-methanol (B)-water (C)-chloromethane The quaternary mixed liq

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  • Alkyl ester method glyphosate solvent recovery system and process
  • Alkyl ester method glyphosate solvent recovery system and process

Examples

Experimental program
Comparison scheme
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Example Embodiment

[0035] Example 1

[0036] A solvent recovery system for the production of glyphosate by alkyl ester method, comprising a dilute methanol solution collection tank 8, a primary distillation tower 9, a methanol methylal solution intermediate tank 13, and a secondary distillation tower 14;

[0037] The glyphosate hydrolysis tail gas pretreatment system produced by the alkyl ester method is connected to the dilute methanol solution collection tank 8. The dilute methanol solution collection tank 8 is connected to the upper part of the primary distillation tower 9 through a pipeline, and the top of the primary distillation tower 9 is condensed A device 10 is connected to a reflux tank 12, and the bottom of the primary distillation tower 9 is connected to the sewage station 20;

[0038] The reflux tank 12 is connected with the methanol methylal solution intermediate tank 13;

[0039] The methanol methylal solution intermediate tank 13 is connected to the secondary rectification tower 14 via a...

Example Embodiment

[0049] Example 2

[0050] A pressure-controlled solvent recovery process for glyphosate produced by alkyl ester method based on the above system, and its specific steps and features are as follows:

[0051] Neutralization and pressure control steps: the mixture of hydrogen chloride, methyl chloride, methanol, methylal, and water vapor from the glyphosate hydrolysis station enters the tail gas neutralization tower together with liquid caustic so as to be neutralized to a pH of 7-10, and the tail gas is removed The acidic components in the gas will then enter the tail gas condenser for condensation and separation after pressure control, the condensate will go to the dilute methanol solution collection tank, and the non-condensable gas will go to the methyl chloride recovery device.

[0052] The pressure of the system where the exhaust gas condenser, the dilute methanol solution collection tank and its pressure balance pipe are controlled by compressor one and compressor two is 0.1-0.4M...

Example Embodiment

[0059] List examples:

[0060] When the selected system pressure P is 0.4MPa and the control system temperature T is in the range of 13-88°C, the above separation effect is achieved.

[0061] When the selected system pressure P is 0.3MPa, the separation requirement can be achieved by controlling the system temperature T in the range of 5-78℃. To give a further example, when the control system pressure P=0.3MPa and the system temperature T is 76-78°C, the water, methanol, and methylal in the tail gas will condense, while the methyl chloride will not be condensed, and the water and methanol in the tail gas will be realized. , Separation of methylal and methyl chloride. The condensate with a temperature of 76-78℃ enters the dilute methanol solution collection tank, and then throttles and reduces to normal pressure (0.1MPa). At this pressure and temperature, the methylal and methanol in the dilute methanol solution enter the first stage The rectification tower vaporizes instantly (th...

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Abstract

The invention provides an alkyl ester method produced glyphosate solvent recovery method. A diluted methanol solution collection tank is connected with the upper part of a primary rectifying tower through a pipeline, and the primary rectifying tower is connected with a return tank I through a condenser I; the return tank I is connected with a methyl alcohol methylal solution intermediate tank; themethyl alcohol methylal solution intermediate tank is connected with a secondary rectifying tank, a return tank II is connected to a methyl alcohol methylal finished product tank, and the secondary rectifying tank is connected to a methyl alcohol finished product tank. The recovery process comprises the following steps: enabling diluted methanol inside the diluted methanol solution collection tank to enter into the primary rectifying tower, enabling gas inside the primary rectifying tower to condense through the condenser to return back to the return tank, and feeding to the methyl alcohol methylal solution intermediate tank; feeding to the methyl alcohol finished product tank from a secondary rectifying tower extraction pump, condensing liquid at the bottom of the tower through the condenser and then feeding to the methyl alcohol finished product tank. According to the equipment and process provided by the invention, the defect that a traditional liquid-phase recovery process highlydepends on a graphite condenser and the problem that a traditional gas-phase recovery process is unstable in operation are solved, the process has the characteristics of energy saving and economical efficiency, and the steam consumption of glyphosate is 1.2t.

Description

technical field [0001] The invention belongs to the technical field of solvent recovery for producing glyphosate by an alkyl ester method. Background technique [0002] Glyphosate is a high-efficiency, low-toxicity, broad-spectrum, destructive, non-selective herbicide with excellent biological characteristics. Currently, there are two mainstream production processes for glyphosate in China: the alkyl ester method and the iminodiacetic acid method. The production process abroad is mainly the iminodiacetic acid method of Monsanto Company in the United States, and the mainstream process for glyphosate production in my country is the alkyl ester method. The alkyl ester method is mainly the glycine-dialkyl phosphite method, and there are also small chloroacetic acid-alkyl ester methods that use chloroacetic acid as the starting material to produce glyphosate and the glycine-trimethyl phosphite method, etc. public routes. [0003] Brief Introduction of Glyphosate Solvent Recove...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D3/14B01D3/42B01D5/00B01D53/68C07C29/74C07C31/04C07C41/58C07C43/30
CPCB01D3/146B01D3/42B01D5/006B01D53/68B01D53/78C07C29/74C07C41/58B01D2257/2045C07C31/04C07C43/30Y02P20/10
Inventor 田义群徐森军曹杰胡波黄明华覃立忠
Owner HUBEI TAISHENG CHEM
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