CO2 hydrate formation promoter
A technology of hydrate formation and accelerator, which is applied in the direction of carbon compounds, reagents, educts, etc., can solve the problems of not many effective and practical ones, and achieve the effects of increasing the formation rate, reducing the pressure of hydrate formation, and increasing the dissolved amount
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0031] This implementation case is that in a reactor with a volume of 60ml, the flue gas (CO 2Concentration 17.0%, N 2 Concentration 83.0%) in CO 2 Hydrates were formed in 25 ml of mixed aqueous solution of tetra-n-butylammonium bromide (TBAB for short, molar concentration of 0.29%) and dodecyltrimethylammonium bromide (DTAB for short, molar concentration of 0.028%). At 1.8°C, under the condition of injected flue gas pressure of 2.53MPa, hydrates are formed at constant volume, and the time taken to form hydrates is 2 minutes, which is two-thirds shorter than that under the same conditions without adding accelerators; at the same time , the gas pressure in the gas phase is 2.18MPa after the generation is complete, CO 2 The amount dissolved in the solution increased by 30% compared with the presence of no promotion. This case shows that under the same conditions, the addition of accelerators can effectively increase the CO 2 The rate of hydrate formation and promote CO 2 Di...
Embodiment 2
[0033] This implementation case is that in a reactor with a volume of 60ml, the flue gas (CO 2 Molarity 17.0%, N 2 Molar concentration 83.0%) in CO 2 Hydrates were formed in 25 ml of mixed aqueous solution of tetra-n-butylammonium chloride (abbreviated as TBAC, with a molar concentration of 0.29%) and dodecyltrimethylammonium bromide (abbreviated as DTAB, with a molar concentration of 0.055%). At 1.8°C, under the condition of injected flue gas pressure of 1.63MPa, CO in the hydrate phase generated by accelerator 2 Compared with the CO in the hydrate phase formed without accelerator 2 The component content is 14.2% higher at 64.0%. This case shows that under the same conditions, the addition of accelerators can effectively increase the production of CO 2 s efficiency.
Embodiment 3
[0035] This implementation case is that in a reactor with a volume of 60ml, the flue gas (CO 2 Molarity 17.0%, N 2 Molar concentration 83.0%) in CO 2 Hydrates are formed in 25 ml of mixed aqueous solutions of tetra-n-octylammonium bromide (abbreviated as TOAB, with a molar concentration of 0.10%) and octadecyltrimethylammonium chloride (abbreviated as STAC, with a molar concentration of 0.014%). At 1.8°C and a pressure of 0.66MPa, gas hydrates are formed in the system with an accelerator, and the component concentration is 56.92%, while no hydrates are formed in the system without an accelerator. This case illustrates that at 1.8°C Under these conditions, the addition of accelerators can effectively reduce the pressure of hydrate formation.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 