Method for co-producing oil fracturing proppant and xonotlite by using high alumina fly ash
A fracturing proppant and high-alumina fly ash technology, which is applied in silicate, earth square drilling, alkaline earth metal silicate, etc., can solve problems affecting wide application, land occupation environment, unfavorable pumping, etc., and achieve Ease of popularization and application, reduction of stockpiling, and avoidance of secondary waste
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0030] The process flow diagram of the co-production of oil fracturing proppant and xonotlite by using high alumina fly ash in this embodiment is as follows figure 1 As shown, the specific steps are:
[0031] 1. Pre-desilication
[0032] Mix high-alumina fly ash with an alumina content of 45% and a sodium hydroxide solution with a concentration of 120g / L at a mass ratio of 0.5:1 between sodium hydroxide and high-alumina fly ash; the mixed slurry formed by mixing Heating to 90°C for 3.0 hours of desiliconization reaction, and solid-liquid separation to obtain desiliconization liquid in liquid phase and desiliconization fly ash in solid phase.
[0033] Among them, the concentration of sodium metaaluminate in the desiliconization solution is 3.6g / L, the concentration of sodium carbonate is 8.6g / L, and the concentration of silicon oxide is 55.0g / L; the chemical composition of desiliconization fly ash includes: alumina 58.7wt%, silicon oxide 27.5wt%, calcium oxide 1.4wt%, iron ox...
Embodiment 2
[0044] The specific steps of utilizing high alumina fly ash to co-produce petroleum fracturing proppant and xonotlite in this embodiment are:
[0045] 1. Pre-desilication
[0046] Mix high-alumina fly ash with an alumina content of 48% and a sodium hydroxide solution with a concentration of 100g / L at a mass ratio of 0.7:1 between sodium hydroxide and high-alumina fly ash; the mixed slurry formed by mixing Heating to 120° C. for 1.0 h of desiliconization reaction, and solid-liquid separation to obtain desiliconization liquid in liquid phase and desiliconization fly ash in solid phase.
[0047] Among them, the concentration of sodium metaaluminate in the desiliconization solution is 2.4g / L, the concentration of sodium carbonate is 10.8g / L, and the concentration of silicon oxide is 62.3g / L; the chemical composition of desiliconization fly ash includes: alumina 61.7wt%, silicon oxide 26.6wt%, calcium oxide 1.7wt%, iron oxide 2.4wt%, sodium oxide 3.8wt%.
[0048] 2. Preparation o...
Embodiment 3
[0058] The specific steps of utilizing high alumina fly ash to co-produce petroleum fracturing proppant and xonotlite in this embodiment are:
[0059] 1. Pre-desilication
[0060] Mix high alumina fly ash with an alumina content of 52% and a sodium hydroxide solution with a concentration of 110g / L at a mass ratio of 0.6:1 between sodium hydroxide and high alumina fly ash; the mixed slurry formed by mixing Heating to 125° C. for 1.0 h of desiliconization reaction, and solid-liquid separation to obtain desiliconization liquid in liquid phase and desiliconization fly ash in solid phase.
[0061] Among them, the concentration of sodium metaaluminate in the desiliconization solution is 1.8g / L, the concentration of sodium carbonate is 11.7g / L, and the concentration of silicon oxide is 66.4g / L; the chemical composition of desiliconization fly ash includes: alumina 63.1wt%, silicon oxide 26.3wt%, calcium oxide 2.6wt%, iron oxide 1.5wt%, sodium oxide 3.5wt%.
[0062] 2. Preparation o...
PUM
| Property | Measurement | Unit |
|---|---|---|
| particle size (mesh) | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
| density | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More 
