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Method for reducing discharge of oxidization raffinate

A technology of discharge and residual liquid, applied in chemical instruments and methods, inorganic chemistry, peroxides/peroxyhydrates/peroxyacids/superoxides/ozone oxides, etc. Affect the oxidation yield of hydrogenated liquid, increase the cost of sewage treatment, etc., to achieve the effect of improving the oxidation yield, overcoming the hidden dangers of safety production, and reducing the loss of sewage

Active Publication Date: 2011-01-26
湖南双阳高科化工有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because the degradants in the oxidation raffinate float above the water phase, phosphoric acid and hydrogen peroxide are also discharged in large quantities while the degraded substances are discharged, which affects the oxidation yield of the hydrogenated liquid, while phosphoric acid and hydrogen peroxide are discharged in large quantities. discharge, causing material loss, increasing the amount of sewage discharged in the production process, and easily causing the phosphorus content in the wastewater to exceed the standard, causing pollution to the environment and increasing the cost of sewage treatment

Method used

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  • Method for reducing discharge of oxidization raffinate
  • Method for reducing discharge of oxidization raffinate
  • Method for reducing discharge of oxidization raffinate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] The oxidation raffinate at the bottom of the upper tower 1 of the oxidation tower is continuously discharged through the upper tower raffinate discharge pipe 4, and the discharged oxidation raffinate enters the bottom of the middle tower 2 and is mixed with the hydrogenated liquid and air entering the middle tower 2 Finally, participate in the chemical reaction in the middle section tower 2, and observe the quality of the oxidation raffinate discharged from the upper section tower raffinate discharge pipe 4 through the sight glass 7 to adjust the opening of the valve 10 and the valve 11, and the upper section tower 1 is oxidized The ratio of the volume of residual liquid discharge to the volume of hydrogenated liquid entering the tower is 1:200; the oxidized raffinate at the bottom of the middle-section tower 2 is continuously discharged through the middle-section tower raffinate discharge pipe 5, and the discharged oxidized raffinate enters the The bottom of the lower t...

Embodiment 2

[0025] The oxidation raffinate at the bottom of the upper section tower 1 of the oxidation tower is intermittently discharged through the upper section tower raffinate discharge pipe 4, and the quality of the oxidation raffinate discharged in the upper section tower raffinate discharge pipe 4 is observed through the sight glass 7 to determine Adjust the closing or opening of valve 10 and valve 11 and their opening degree, first discharge the water-phase substance in the oxidation raffinate from the upper section tower raffinate discharge pipe 4 into the middle section tower 2, and then pass the oxidation raffinate degradation product through The bypass discharge pipe 18 for the raffinate of the upper tower is discharged out of the oxidation tower, and the water-phase substance in the discharged oxidation raffinate enters the bottom of the middle tower 2, mixes with the hydrogenated liquid and air entering the middle tower 2, and is discharged in the middle tower Participate in...

Embodiment 3

[0027] The oxidation raffinate at the bottom of the upper tower 1 of the oxidation tower is continuously discharged through the upper tower raffinate discharge pipe 4, and the discharged oxidation raffinate enters the bottom of the middle tower 2 and is mixed with the hydrogenated liquid and air entering the middle tower 2 Finally, participate in the chemical reaction in the middle section tower 2, and observe the quality of the oxidation raffinate discharged from the upper section tower raffinate discharge pipe 4 through the sight glass 7 to adjust the opening of the valve 10 and the valve 11, and the upper section tower 1 is oxidized The volume ratio of the amount of raffinate discharge to the amount of hydrogenated liquid entering the section tower is 1:250; the oxidized raffinate at the bottom of the middle section tower 2 is intermittently discharged through the middle section tower raffinate discharge pipe 5, and observed through the sight glass 8 The quality of the oxida...

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Abstract

The invention provides a method for reducing the discharge of oxidization raffinate, comprising the following steps of: discharging the oxidization raffinate in an upper tower of an oxidization tower to the bottom of a middle tower through an upper tower raffinate discharging pipe so that the oxidization raffinate is mixed with hydrogenation liquid and air entering the middle tower; discharging the oxidization raffinate in the middle tower to the bottom of a lower tower through a middle tower raffinate discharging pipe so that the oxidization raffinate is mixed with hydrogenation liquid and air entering the lower tower; and discharging out the oxidization raffinate at the bottom of the lower tower through a lower tower raffinate discharging pipe, adding water to dilute the oxidization raffinate and then sending to a sewage treatment system. The invention has the functions of improving the oxidization yield of the hydrogenation liquid, reducing the consumption of materials such as phosphoric acid and the like, reducing the product cost of the sewage treatment and improving the product quality, and is beneficial for the solving of the safety problem in the oxidization process when producing hydrogen peroxide by using an anthraquinone method.

Description

technical field [0001] The invention relates to a production method for producing hydrogen peroxide by an anthraquinone method, in particular to a production method for oxidizing hydrogenated liquid. Background technique [0002] The development of hydrogen peroxide production methods in my country has roughly experienced three development stages: electrolysis, nickel catalyst stirred tank hydrogenation process anthraquinone method and palladium catalyst fixed bed hydrogenation process anthraquinone method. The anthraquinone method of the hydrogenation process is the main production method. Chinese patent application number 200710113082.0, date of application November 2, 2007, date of publication May 14, 2008, the patent application titled "A Method for Producing Hydrogen Peroxide by Anthraquinone Method" discloses a method for producing hydrogen peroxide by anthraquinone method The method comprises the steps of putting a palladium catalyst into a hydrogenation tower to pass...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B15/023
Inventor 冯礼义刘光昌黄丰杨云强
Owner 湖南双阳高科化工有限公司
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