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

Integrated technology for capturing and mineralizing carbon dioxide

A carbon dioxide and process technology, applied in the field of carbon dioxide capture and mineralization integrated process, can solve the problems of low recycling rate, large energy consumption, high energy consumption for regeneration, and achieve the goal of reducing use, reducing water consumption and high leaching rate. Effect

Inactive Publication Date: 2012-11-28
HUANENG CLEAN ENERGY RES INST
View PDF5 Cites 15 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] For the traditional carbon dioxide mineralization technology, it is first necessary to use high-temperature heat treatment (600-650°C) and fine grinding (ore particle size less than 38m) for ore activation. -200°C, 150-185bar) to feed the captured gas CO 2 Carry out carbonation reaction, the reaction rate is 78-90% carbonation rate in 1 hour, NaHCO needs to be added in the reaction 3 and NaCl to improve the reaction efficiency, but NaHCO 3 extremely low recycling rate
Another indirect mineralization process using strong acid and strong alkali, first dissolves the ore with strong acid to obtain calcium and magnesium ion leaching solution, and then carries out carbonation reaction with strong alkali. The strong acid and strong alkali required by this process are recycled and regenerated by electrolysis. Very high energy consumption

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

[0023] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:

[0024] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of less than 1mm by a pulverizer, and then ground by a ball mill to a mineral powder of less than 75μm. The ore is serpentine. Solid waste for fly ash;

[0025] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 50g / l, the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1.4:1. The reaction conditions for ore leaching are 100 ℃, the water vapor pressure is 1 bar, the stirring rate is 800-1200 rpm, and the reaction time is 1 hour. The mud obtained after dissolving the ore is passed through a hydrocyclone or The sedimentation tank realizes solid-liquid separation, and t...

Embodiment 2

[0032] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:

[0033] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of less than 1.5mm by a pulverizer, and then ground by a ball mill to a mineral powder of less than 150μm. The ore is olivine, and the solid waste For steel slag;

[0034] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 100g / l, and the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1.2:1. The reaction conditions for ore leaching are 135°, water vapor pressure 3bar, stirring speed 800-1200rpm, reaction time 1 hour, and the mud obtained after dissolving the ore passes through the hydrocyclone Or the sedimentation tank realizes solid-liquid separation, and the separ...

Embodiment 3

[0041] An integrated process of carbon dioxide capture and mineralization, comprising the following steps:

[0042] In the first step, the ore or other bulk solid waste rich in calcium and magnesium ions is crushed into solid particles with a particle size of 2 mm, and then ground to 300 μm ore powder by a ball mill. The ore is serpentine, and the solid waste is steel slag ;

[0043] In the second step, the ore powder is mixed with ammonium bisulfate (NH 4 HSO 4 ) solution reaction, the solid-liquid ratio of the feed is 150g / l, and the corresponding NH 4 HSO 4 Solution molarity according to NH 4 HSO 4 The molar ratio of magnesium ions in the ore is 1:1. The reaction conditions for ore leaching are 150°, water vapor pressure 4bar, stirring speed 800-1200rpm, reaction time 1 hour, and the mud obtained after dissolving the ore passes through the hydrocyclone Or the sedimentation tank realizes solid-liquid separation, and the separated tailings are coarse silicon powder with...

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

PropertyMeasurementUnit
particle diameteraaaaaaaaaa
particle diameteraaaaaaaaaa
particle diameteraaaaaaaaaa
Login to View More

Abstract

The invention relates to an integrated technology for capturing and mineralizing carbon dioxide, which is characterized in that renewable ammonium salt (NH4HSO4) is used for obtaining a calcium and magnesium ions-containing leachate from ores or solid wastes, the leached residual slag is a small-size particle with high content of silicon oxide, the leachate is subjected to separation, impurities removal and precious metal purification, partial solution is directly used for capturing renewable ammonia gas to obtain a calcium and magnesium containing ammonia-rich liquid, CO2 is captured by the ammonia-rich liquid under normal temperature to generate ammonium carbonate salt, then the ammonium carbonate salt is subjected to rapid reaction with another part of the leachate for depositing to obtain magnesium(calcium) salt product with high purity, and a reaction-finished solution is further heated to regenerate ammonium salt (NH4HSO4) and ammonia gas for pretreating ores and capturing CO2. According to the invention, the steps of the technology enable complete closed circulation, thereby the chemical agent amount and three wastes are reduced, two high energy consumption steps of CO2 capturing desorption and compression in a traditional method can be avoided, the efficiency for each step is more than 90%, the waste heat in a power plant can be simultaneously used for assisting the regeneration of ammonium salt, and total energy consumption of the technology can be reduced.

Description

technical field [0001] The invention relates to the technical field of flue gas carbon dioxide capture and utilization, in particular to an integrated process of carbon dioxide capture and mineralization. Background technique [0002] The global greenhouse effect caused by the increase in the concentration of greenhouse gases in the atmosphere has caused icebergs to melt, sea levels to rise, species to decrease, and various climate disasters to occur frequently around the world, causing serious economic losses and threatening human survival. carbon dioxide (CO 2 ) As the most important greenhouse gas, its future total control and emission rights allocation have become the focus of international climate negotiations. Governments and energy companies in various countries have paid more and more attention to CO 2 Research on emission control technologies, some countries have taken the lead in starting substantive decarbonization work. With my country's carbon emissions surpa...

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 Applications(China)
IPC IPC(8): B01D53/78B01D53/62C01B33/113C01G49/06C01F5/24C01F11/18
CPCY02C10/04Y02C20/40Y02P20/129Y02P20/151
Inventor 王晓龙许世森郜时旺刘练波王金意
Owner HUANENG CLEAN ENERGY RES INST
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