Technological method for producing high-purity low-iron aluminum sulfate by using coal ash and comprehensively utilizing coal ash
A technology of low-iron aluminum sulfate and process method, which is applied in the fields of aluminum sulfate, cement production, aluminum-sulfur compounds, etc., and can solve the problem of many aluminum sulfate crystals, high impurity components in aluminum sulfate products, and difficulty in preparing high-purity low-iron aluminum sulfate products, etc. problems, and achieve the effect of low cost and remarkable benefits of comprehensive utilization
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0039] Embodiment 1: raw material fly ash is composed of: Al 2 o3 Content 37.7%, Fe 2 o 3 Content 4.38%, CaO content 3.74%, MgO content 0.54%, SiO 2 The content is 49.9%, and the loss on ignition is 1.92%. The raw fly ash can also use other components and their corresponding amounts.
[0040] Mill the fly ash in a ball mill for 1 hour to perform mechanical activation; add water according to the mass ratio of fly ash to water of 1:3, fully stir, remove unburned black through flotation; and remove iron oxide through magnetic separation; The fly ash residue after flotation carbon and magnetic separation of iron and concentrated sulfuric acid are made into a mixed solution with a sulfuric acid concentration of 40%. The solid-liquid ratio of the fly ash and the mixed solution is controlled to be 1:8. Heating and pressurizing the reaction for 3 hours, the highest temperature of the reaction is 240 °C; after the reaction cools down, add water according to the mass ratio of fly as...
Embodiment 2
[0044] Embodiment 2: with the fly ash in embodiment 1, ball mill 2h in ball mill, carry out mechanical activation; According to the mass ratio of fly ash and water is 1: 3, add water, fully stir, remove unburned net through flotation black; then remove the iron oxide by magnetic separation; make a mixed solution with a sulfuric acid concentration of 50% from the fly ash residue after the flotation of carbon and magnetic iron with concentrated sulfuric acid, and control the solid-liquid mixture of the fly ash and the mixed solution The ratio is 1:7, heat and pressurize the reaction for 4 hours in the acid-resistant reaction equipment, the highest temperature of the reaction is 240 ° C; The filter cake was obtained by filtration, and washed with water with a mass ratio of fly ash to water of 1:1 to obtain a crude aluminum sulfate solution. The extraction rate of aluminum analyzed was 75%.
[0045] Evaporate and concentrate the crude aluminum sulfate solution at 110°C to 1 / 10 of...
Embodiment 3
[0047] Embodiment 3: with the fly ash in embodiment 1, ball mill 3h in ball mill, carry out mechanical activation; According to the mass ratio of fly ash and water is 1: 2, add water, fully stir, remove unburned net through flotation black; and then remove iron oxide by magnetic separation; make a mixed solution with a sulfuric acid concentration of 80% from the fly ash residue after flotation carbon and magnetic iron separation and concentrated sulfuric acid, and control the solid-liquid concentration of fly ash and the mixed solution Ratio of 1:6, heating and pressurizing reaction in acid-resistant reaction equipment for 5h, the highest temperature of the reaction is 240°C; The filter cake was obtained by filtration, and washed with water with a mass ratio of fly ash to water of 1:2 to obtain a crude aluminum sulfate solution. The extraction rate of aluminum analyzed was 72%.
[0048] Evaporate and concentrate the aluminum sulfate crude liquid at 100°C to 1 / 10 of the origin...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com