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Method for producing nano silicon dioxide and nano calcium carbonate by using rice hull ash and flue gas of biomass power plant

A nano-silica, nano-calcium carbonate technology, applied in the direction of silica, nanotechnology for materials and surface science, silicon oxide, etc., can solve the problem that it is difficult to achieve nano-silica, low dissolution rate of silica , industrialization difficulties and other problems, to achieve the effect of reducing waste, saving equipment investment and simple operation

Active Publication Date: 2014-04-02
ZHONGYING CHANGJIANG INTERNATIONAL NEW ENERGY INVESTMENT CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the above-mentioned each method, or rice husk ash adds soda ash under the normal pressure condition, produces water glass and then cools down and directly precipitates silicon dioxide, and the industrialization of this method is difficult
Or rice husk ash and caustic soda are used to produce water glass under high temperature and high pressure conditions, the dissolution rate of silicon dioxide is low, and in the process of preparing silicon dioxide by acidification of water glass, the silicon dioxide is obtained by directly acidifying sodium silicate. Acid and silicic acid aggregates are precipitated and separated from the system. In fact, the aggregation process of silicic acid is a process in which the particles grow gradually, that is, through the process of sol, gel, and precipitation. If the particles are allowed to aggregate and grow naturally, in fact Difficult to reach nano-silica with very small particle size

Method used

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  • Method for producing nano silicon dioxide and nano calcium carbonate by using rice hull ash and flue gas of biomass power plant

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] (1) Take the rice husk ash (SiO 2 Content 90wt%, BET specific surface area 60m 2 / g, SiO 2 Crystal structure: amorphous) 74kg, adding concentration is 15wt% in the sodium hydroxide solution, wherein: the mass ratio of rice husk ash: sodium hydroxide in the sodium hydroxide solution is 2.8:1, under stirring condition, heat up to 96 0 C, heat preservation reaction for 3.5 hours, filter;

[0022] (2) Put the filtrate of step (1) in the reaction kettle, add water to dilute, control the mass percentage concentration of sodium silicate in the solution to be 15% in terms of silicon dioxide, and then raise the temperature to 70 0 C, add dispersant PEG2000 (polyethylene glycol 2000), add-on is 1kg, under normal pressure condition, continuously pass into the flue gas of biomass power plant, the volume content of carbon dioxide in the flue gas is 12-20% ( v / v), the access rate is 300m 3 / h, heat preservation reaction for 2.5 hours, stop passing the flue gas, stir and mature fo...

Embodiment 2

[0026] (1) Take the rice husk ash (SiO 2 Effective content 80wt%, BET specific surface area 100m 2 / g, SiO 2 Crystal structure: amorphous) 74kg, adding concentration is 12wt% in the sodium hydroxide solution, wherein: rice husk ash: the mass ratio of sodium hydroxide in the sodium hydroxide solution is 2.6:1, under stirring condition, heat up to 97 0 C, heat preservation reaction for 3.0 hours, filter;

[0027] (2) Put the filtrate of step (1) in the reaction kettle, add water to dilute, control the concentration of sodium silicate in the solution to 10% by mass percentage in terms of silicon dioxide, and raise the temperature to 65 0 C, add dispersant PEG3000, the addition amount is 1kg, and then under normal pressure conditions, continue to pass into the flue gas of the biomass power plant, the flow rate is 500m 3 / h, the volume content of carbon dioxide in the flue gas is 12-20% (v / v), heat preservation reaction for 2.0 hours, stop the flow of flue gas, stir and mature f...

Embodiment 3

[0032] (1) Take the rice husk ash (SiO 2 Effective content 90wt%, BET specific surface area 100m 2 / g, SiO 2 Crystal structure: amorphous), adding the concentration of 10wt% sodium hydroxide solution, under stirring conditions, heating up to 98 0C, keep warm and fully react for 3.0 hours, filter;

[0033] (2) Place the filtrate of step (1) in a reaction kettle, add water to dilute, control the concentration of sodium silicate in the solution to 8% by mass in terms of silicon dioxide, and raise the temperature to 60 0 C, adding dispersant PEG3000, the amount of dispersant added is 0.5wt% of sodium silicate in the filtrate obtained in step (1) based on the mass of silicon dioxide, and then under normal pressure conditions, continue to feed the raw material after purification treatment Flue gas from a material power plant with an inflow rate of 250m 3 / h, the volume content of carbon dioxide in the flue gas is 12-20% (v / v), keep warm for 3.5 hours, stop passing the flue gas, ...

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Abstract

The invention relates to a method for producing nano silicon dioxide and nano calcium carbonate by using rice hull ash and flue gas of a biomass power plant. The method comprises the following steps: adding the rice hull ash, obtained by combustion in the biomass power plant for power generation, into 10-20% sodium hydroxide solution by weight, fully reacting the mixture at the temperature of 95-1,000 DEG C for 3-4 hours, and performing filtration; adding water into filtrate to dilute the filtrate, controlling sodium silicate in a system to be 8-15 percent by mass in silicon dioxide, heating to 60-800 DEG C, adding a dispersing agent, continuously feeding the flue gas of the biomass power plant under a normal pressure condition, fully stirring to react for 2-4 hours to obtain the nano silicon dioxide; mixing the filtrate and washing liquor, adding a calcium hydroxide solution at the temperature of 5-700 DEG C, and fully stirring to react for 0.5-2 hours to obtain the nano calcium carbonate. The particle sizes of the silicon dioxide product and the nano calcium carbonate product which are obtained by the method are extremely small and can both reach the nano level.

Description

technical field [0001] The invention relates to a method for producing nano-materials by recycling waste residue and waste gas of a biomass power plant, in particular to a method for producing nano-materials by utilizing waste rice husk ash after burning rice husks for power generation in a biomass power plant and flue gas when burning rice husks. Methods of silicon oxide and nano calcium carbonate. Background technique [0002] At present, there are many methods for recycling rice husk ash as renewable resources, such as patent CN1756719, which uses rice husk ash and carbon dioxide as raw materials to produce silica. In this method, the leaching rate of silica is low, about 70%, and two The synthetic reaction of silicon oxide is carried out under pressurized conditions, the operation is difficult, and the equipment investment is large; the patent CN1762802 uses rice husk ash to cook with alkali under high temperature and pressure to produce water glass, and then reacts wate...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B33/12C01F11/18B82Y30/00
CPCB82Y40/00C01B33/12C01B33/18C01F11/18C01F11/183C01P2004/64C01P2006/80B82Y30/00C01F11/181
Inventor 陈义龙张岩丰卓之久郑兴才方章建陶磊明程宇婷
Owner ZHONGYING CHANGJIANG INTERNATIONAL NEW ENERGY INVESTMENT CO LTD
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