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Method and device for controlling feeding in bromine process

A technology of feeding control and control device, applied in program control, electrical program control, program control in sequence/logic controller, etc., can solve the problems of low degree of automation and low accuracy, so as to improve the extraction rate and realize accurate Control and improve the effect of working environment

Inactive Publication Date: 2018-09-04
山东金特装备科技发展有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The purpose of the present invention is to solve the technical problems of low accuracy and low degree of automation in the feeding control of bromine production in the prior art, and to provide a feeding control method and device in the bromine process

Method used

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  • Method and device for controlling feeding in bromine process
  • Method and device for controlling feeding in bromine process
  • Method and device for controlling feeding in bromine process

Examples

Experimental program
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Embodiment 1

[0038] This example is used to illustrate the theoretical basis for maintaining the Eh value of the oxidation-completed liquid within the range of 880-1100 mV. In this embodiment, the Eh value is determined through a simulation experiment.

[0039] Chlorine gas is introduced into the oxidation tower, and the chemical reaction that occurs is:

[0040]

[0041] HCl+HClO+2NaBr→2NaCl+Br 2 ↑+H 2 O (2)

[0042] Chlorine reacts with water to produce hydrochloric acid and hypochlorous acid (Equation 1), the latter converting Br - The ions are oxidized to generate free bromine (Formula 2), and the free bromine is brought to the absorption tower by the blown air in the blow-out tower.

[0043] From the perspective of reaction equilibrium constant, chlorine should be moderately excessive to ensure that formula (2) can be carried out more thoroughly. If too much chlorine is present in excess, the following reactions may occur:

[0044] NaBr+3HClO=NaBrO 3 +3HCl (4)

[0045] If b...

Embodiment 2

[0051] This example is used to illustrate the theoretical basis for maintaining the Eh value in the blowing tower drainage within the range of 340-560mV. In this embodiment, the Eh value is determined through a simulation experiment.

[0052] In the absorption process of the air blowing method, SO is first added to the eluent 2 (generated by burning sulfur), generating sulfurous acid, free bromine is reduced to bromide ion by sulfurous acid, and absorbed by eluent, the reaction formula is:

[0053] SO 2 +H 2 O=H 2 SO 3 (5)

[0054] Br 2 +H 2 SO 3 +H 2 O=2HBr+H 2 SO 4 (6)

[0055] If the absorption process has not been completed, SO 2 Will be absorbed in the eluent, if the free bromine has not been completely reduced, SO 2 will escape and enter the subsequent absorption liquid. For example, after passing through the trapping tower and returning to the blowing tower, the SO 2 It will enter the drain of the blow-out tower. In the actual production process, it i...

Embodiment 3

[0059] In this example, simulation experiments will be used to demonstrate the influence of the pH value of the oxidation-completed liquid before purging on the stripping rate, so as to illustrate the theoretical basis for maintaining the pH value of the oxidation-completed liquid at 2.5-4. At the same time, in this embodiment, two kinds of purge gases are set as a comparison, which are CO and N respectively. 2 .

[0060] 1. Solution configuration

[0061] Solution 1 (100mL): 10% NaCl, 0.5gNaBr (concentration at this time is 5000mg / L)

[0062] Solution 2: hypochlorous acid solution (containing 0.05% hypochlorous acid)

[0063] 2. Experimental steps

[0064] 2.1) Configure 100mL solution 1, adjust its pH value to 2 with concentrated hydrochloric acid and 1M NaOH solution, and simultaneously adjust the pH value of solution 2 to 2 with concentrated hydrochloric acid and 1M NaOH solution;

[0065] 2.2) Add dropwise solution 2 with the same pH value to solution 1, measure the E...

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Abstract

The invention discloses a method and device for controlling feeding in the bromine process, and belongs to the field of bromine production. The method is applied to the production process of bromine extraction performed according to an air blow-out method. The method comprises the steps of continuously monitoring an Eh value of an oxidation completion solution in the bromine extracting process, and monitoring an Eh value of a receiving solution after the excessive unabsorbed SO2 is discharged out of the tower body in an absorption tower at the same time; enabling the Eh value of the oxidationcompletion solution to be kept at 880-1100mV through adjusting the chlorine input volume in a chlorine oxidation procedure; and enabling the Eh value of the receiving solution to be kept at 340-560mVthrough adjusting the SO2 input volume in an absorption procedure. According to the invention, the bromine production process can be monitored by detecting a plurality of parameters at different positions on a process line through an electrode, a judgment standard is provided for feedback control, and the bromine productivity is improved.

Description

technical field [0001] The invention belongs to the field of bromine production, and in particular relates to a feeding control method and device in a bromine process. Background technique [0002] As an important chemical raw material, bromine is widely used in chemical, pharmaceutical, pesticide, and petroleum industries, and plays an important role in the development of my country's national economy and science and technology. At present, there are two classic methods for bromine extraction: steam distillation method and air blowing method, as well as ion exchange resin method, membrane separation method, adsorption, electrolysis, electrosorption, air oxidation, acid oxidation and other methods. The steam distillation method is suitable for extracting bromine from high-concentration brine. This method was widely used in northern my country in the early 1970s. However, due to the low annual output and limited to brine with high bromine content, it was gradually replaced by...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G05B19/418G05B19/05G05B19/04C01B7/09
CPCC01B7/09G05B19/04G05B19/056G05B19/41835Y02P90/02
Inventor 黄元凤王秋瑾谢亚平张冰李士波刘丹王震叶瑛曹怀祥秦华伟张平萍
Owner 山东金特装备科技发展有限公司