Individualized risk vehicle matching for an on-demand transportation service
US-2018341887-A1 · Nov 29, 2018 · US
US11858865B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11858865-B2 |
| Application number | US-202217840809-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 15, 2022 |
| Priority date | Mar 18, 2019 |
| Publication date | Jan 2, 2024 |
| Grant date | Jan 2, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided herein are compositions and methods of carbonation processing for the fabrication of cementitious materials and concrete products. Embodiments include manufacturing processes of a low-carbon concrete product comprising: forming a cementitious slurry including portlandite; shaping the cementitious slurry into a structural component; and exposing the structural component to a CO 2 waste stream, thereby enabling manufacture of the low-carbon concrete product.
Opening claim text (preview).
What is claimed is: 1. A manufacturing process of a low-carbon concrete product, comprising: forming a cementitious slurry including portlandite; shaping the cementitious slurry into a structural component, wherein shaping the cementitious slurry comprises compacting the cementitious slurry at a pressure in a range of about 0.5 MPa to about 50 MPa; and exposing the structural component to a post-combustion or post-calcination flue gas stream containing CO 2 , thereby enabling manufacture of the low-carbon concrete product. 2. The manufacturing process of claim 1 , wherein forming the cementitious slurry includes combining water and a binder including the portlandite and optionally cement and coal combustion residuals at a water-to-binder mass ratio (w/b) of about 0.5 or less. 3. The manufacturing process of claim 2 , wherein w/b is about 0.45 or less. 4. The manufacturing process of claim 1 , wherein forming the cementitious slurry includes combining water and a binder including a cement, portlandite, and coal combustion residuals, at a mass percentage of the cement in the binder of about 25% or greater and up to about 50%. 5. The manufacturing process of claim 4 , wherein the mass percentage of the cement in the binder is about 30% or greater. 6. The manufacturing process of claim 1 , further comprising drying the structural component prior to exposing the structural component to the post-combustion or post-calcination flue gas stream containing CO 2 . 7. The manufacturing process of claim 6 , wherein drying the structural component includes reducing a degree of pore water saturation (S w ) to less than 1. 8. The manufacturing process of claim 7 , wherein S w is about 0.9 or less. 9. The manufacturing process of claim 6 , wherein drying the structural component includes reducing S w to a range of about 0.1 to about 0.7. 10. The manufacturing process of claim 6 , wherein drying the structural component is performed at a temperature in a range of about 20° C.to about 85° C., for a time duration in a range of 1 h to about 72 h. 11. The manufacturing process of claim 1 , wherein compacting the cementitious slurry includes reducing a degree of water saturation (S w ) to less than 1. 12. The manufacturing process of claim 11 , wherein S w is about 0.9 or less. 13. The manufacturing process of claim 11 , wherein compacting the cementitious slurry includes reducing S w to a range of about 0.1 to about 0.7. 14. The manufacturing process of claim 1 , wherein exposing the structural component to the post-combustion or post-calcination flue gas stream containing CO 2 is performed at ambient pressure and at a temperature in a range of about 20° C. to about 80° C. 15. The manufacturing process of claim 1 , wherein the low-carbon concrete products have up to 75% lower embodied carbon intensity than a traditional cement-based concrete product. 16. The manufacturing process of claim 15 , wherein the lower carbon intensity is due to (a) partial substitution of cement with portlandite and/or fly ash and/or (b) CO 2 uptake during manufacturing.
Carbon dioxide sequestration · CPC title
Carbon dioxide hardening · CPC title
Lime {(obtaining Ca(OH)2 otherwise than by simple slaking of quick lime C01F11/02)} · CPC title
Hardening promoted by a rise in temperature (C04B40/024 takes precedence) · CPC title
Portland cements · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.