Looking for breakthrough ideas for innovation challenges? Try Patsnap Eureka!

Recovery method for iodine from wet-process phosphoric acid at low gas-liquid ratio

A wet-process phosphoric acid and iodine recovery technology, which is applied in the directions of iodine, iodine/hydrogen iodide, etc., can solve the problems of increased investment cost of extraction device equipment construction, increased energy consumption and cost, increased size of extraction tower, etc., and can reduce equipment Investment cost, power consumption reduction, effect of reducing investment cost

Inactive Publication Date: 2015-04-01
贵州开磷碘业有限责任公司
View PDF4 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But this method has some disadvantages
First of all, since iodine molecules are blown out by hot air at a temperature of 40-50°C during extraction, the air must be heated before it enters the extraction tower, and even heat exchange equipment is added, which leads to increased energy consumption and cost
Secondly, the gas-liquid ratio in the air blowing process of this method is 130-150:1, which is relatively large and requires a large amount of air, so it is necessary to use a fan with a large air volume and high motor power, resulting in increased cost investment, and Increased operating costs and reduced economic benefits
Thirdly, due to the relatively large gas-liquid ratio, the specification of the extraction tower is required to increase accordingly, resulting in an increase in the investment cost of the extraction equipment construction

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] (1) After filtering the iodine-containing dilute phosphoric acid produced in the production process of wet-process phosphoric acid at a temperature of 80°C, take 1m 3 Put it into an oxidation tank, add hydrogen peroxide and carry out a chemical reaction for 10 minutes, so that ionic iodine is oxidized into free molecular iodine, and the iodine content after oxidation is 41mg / L; the volume ratio of the hydrogen peroxide and iodine-containing dilute phosphoric acid is 0.05:100;

[0020] (2) (2) Slowly and evenly pump the oxidized iodine-containing phosphoric acid into the extraction tower, enter and spray into the tower from the upper part of the extraction tower;

[0021] (3) Use a blower to blow air at room temperature for 30m 3 Slowly and evenly send into the extraction tower from the lower part of the extraction tower, the volume of air is 30 times the volume of dilute phosphoric acid, that is, the gas-liquid ratio is 30:1;

[0022] (4) The iodine-containing dilute p...

Embodiment 2

[0024] (1) After filtering the iodine-containing dilute phosphoric acid produced in the production process of wet-process phosphoric acid at a temperature of 75°C, take 5m 3 Put it into an oxidation tank, add hydrogen peroxide to carry out chemical reaction for 20 minutes, so that ionic iodine is oxidized into free molecular iodine, and the iodine content after oxidation is 38mg / L; the volume ratio of the hydrogen peroxide and iodine-containing dilute phosphoric acid is 0.1:100;

[0025] (2) Slowly and evenly send the oxidized iodine-containing phosphoric acid into the extraction tower with a pump, enter and spray into the tower from the top of the extraction tower;

[0026] (3) Use the blower to blow the normal temperature air 200m 3 Slowly and evenly send into the extraction tower from the lower part of the extraction tower, the volume of air is 40 times the volume of dilute phosphoric acid, that is, the gas-liquid ratio is 40:1;

[0027] (4) The iodine-containing dilute ph...

Embodiment 3

[0029] (1) After filtering the iodine-containing dilute phosphoric acid produced in the production process of wet-process phosphoric acid at a temperature of 70°C, take 10m 3 Put it into an oxidation tank, add hydrogen peroxide and carry out a chemical reaction for 35 minutes, so that ionic iodine is oxidized into free molecular iodine, and the iodine content after oxidation is 43mg / L; the volume ratio of the hydrogen peroxide and iodine-containing dilute phosphoric acid is 0.15:100;

[0030] (2) Slowly and evenly send the oxidized iodine-containing phosphoric acid into the extraction tower with a pump, enter and spray into the tower from the top of the extraction tower;

[0031] (3) Use the blower to blow the normal temperature air 600m 3 Slowly and evenly send into the extraction tower from the lower part of the extraction tower, the volume of air is 60 times the volume of dilute phosphoric acid, that is, the gas-liquid ratio is 60:1;

[0032] (4) The iodine-containing dilu...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention discloses a recovery method for iodine from wet-process phosphoric acid at a low gas-liquid ratio. The recovery method comprises the following steps: adding hydrogen peroxide into dilute phosphoric acid produced from phosphoric acid by a wet process and allowing hydrogen peroxide to react with dilute phosphoric acid; then blowing out molecular iodine by using air; absorbing molecular iodine by using an acidic solution; and finally adding hydrogen peroxide to allow iodine to be precipitated. The method is characterized in that molecular iodine is blown out by using normal temperature air and a volume ratio of blown air to liquid, i.e., a gas-liquid ratio, is low. The method has the following advantages: energy consumption is lowered down, layout of equipment is reduced, and investment cost is decreased; a gas-liquid ratio in blowing-out of molecular iodine by using a conventional extraction process for iodine from wet-process phosphoric acid is substantially decreased, fan delivery is reduced, investment cost for equipment is lowered down, and due to decrease of fan delivery, power consumption in the process of operation and operation cost are reduced; moreover, the low gas-liquid ratio enables the boundary dimension of an extraction tower to be effectively reduced and construction and maintenance cost for an apparatus to be substantially decreased.

Description

technical field [0001] The invention relates to a method for recovering iodine from wet process phosphoric acid with low gas-liquid ratio. Background technique [0002] With the development of industry and agriculture, iodine has been widely used in medicine and health, agriculture, industry, national defense and other aspects. At present, the extraction method of iodine mainly uses seaweed, brine and minerals (phosphate rock) as raw materials. The methods for extracting iodine mainly include dry distillation, leaching, ion exchange, solvent extraction, electrolysis, liquid membrane technology, and air blowing. Among them, the air blowing method is a relatively advanced production process. The air blowing method is initially applicable to the stock solution with high iodine content, mainly brine. The process is to first acidify the iodine-containing mother liquor with hydrochloric acid to a pH value of 1-2, and then introduce chlorine gas for oxidation to oxidize ion iodi...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C01B7/14
Inventor 徐魁廖吉星周勇王先炜何国勇杨俊杰唐明亮
Owner 贵州开磷碘业有限责任公司
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Patsnap Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Patsnap Eureka Blog
Learn More
PatSnap group products