Method and apparatus for sustainable carbon dioxide sequestration
US-2024424442-A1 · Dec 26, 2024 · US
US9278307B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9278307-B2 |
| Application number | US-201313900269-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 22, 2013 |
| Priority date | May 29, 2012 |
| Publication date | Mar 8, 2016 |
| Grant date | Mar 8, 2016 |
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The use of a composition that includes a metal salt and an oil soluble amine formaldehyde reaction product scavenges H 2 S that is present in aqueous fluids (e.g. produced water liquid streams), natural gas and in oil and mixtures thereof (e.g. mixed production streams that contain all three phases) better than either component when used alone. The resulting scavenger combination significantly increases the reaction rate and the overall scavenging efficiency, i.e. capacity over each component when used alone, in the same total amount. Non-limiting examples of the metal salt include zinc or iron carboxylates, and a non-limiting example of an oil soluble amine formaldehyde reaction product is the reaction product of dibutylamine with formaldehyde.
Opening claim text (preview).
What is claimed is: 1. A method for scavenging hydrogen sulfide from a fluid selected from the group consisting of an aqueous phase, a gaseous phase, a hydrocarbon phase and mixtures thereof, the method comprising contacting the fluid with a composition in an effective amount for synergistically scavenging hydrogen sulfide, where the composition comprises: zinc octoate, and dibutylamine formaldehyde reaction product; where synergistically scavenging is defined as the amount of hydrogen sulfide scavenged is greater as compared with an amount scavenged using a composition of the sum of the components when used separately. 2. The method of claim 1 where the composition comprises from about 0.0001 wt % to about 99 wt % metal salt, where the balance is dibutylamine formaldehyde reaction product. 3. The method of claim 1 where the effective amount of the composition present in the fluid is from about 10 to about 10,000 ppm. 4. The method of claim 1 where the method is practiced in a refinery. 5. The method of claim 1 where the method is practiced in upstream production. 6. A method for scavenging hydrogen sulfide from a fluid selected from the group consisting of an aqueous phase, a gaseous phase, a hydrocarbon phase and mixtures thereof, the method comprising contacting the fluid with from about 10 to about 10,000 ppm of a composition for synergistically scavenging hydrogen sulfide, where the composition comprises: from about 0.0001 wt % to about 99 wt % zinc octoate, and where the balance is dibutylamine formaldehyde reaction product; where synergistically scavenging is defined as the amount of hydrogen sulfide scavenged is greater as compared with an amount scavenged using a composition of the sum of the components when used separately. 7. The method of claim 6 where the method is practiced in a refinery. 8. The method of claim 6 where the method is practiced in upstream production.
Removing hydrogen sulfide · CPC title
Organic sulfur compounds, e.g. mercaptans · CPC title
Hydrogen sulfide · CPC title
Secondary amines · CPC title
Selection of liquid materials for use as absorbents · CPC title
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