Conditioned curing systems and processes thereof

Patent metadata

Field	Value
Publication number	US-11034625-B2
Application number	US-201715609908-A
Country	US
Kind code	B2
Filing date	May 31, 2017
Priority date	May 31, 2016
Publication date	Jun 15, 2021
Grant date	Jun 15, 2021

Abstract

The invention provides novel apparatus and processes for gas flow and conditioning to achieve optimal CO2 curing of articles of composite materials (e.g., precast objects made of carbonatable calcium silicate-based cements), with solid interior or having hollow interior ducts, channels and chambers or otherwise being hollowed out, as well as the precast objects so made, which are suitable for a variety of applications in construction, pavements and landscaping, and infrastructure.

First claim

The invention claimed is:

1. A process for curing a precast object, comprising:
introducing the precast object into an envelope that is capable of containing a gas, the envelope having a first end and a second end, wherein the envelope is sealed or vented;
providing a primary gas circulation loop, comprising:
introducing a gas at a first condition into the envelope,
flowing the gas over a surface of the precast object inside the envelope to bring the gas to a second condition,
passing the gas at the second condition through a primary gas conditioning system to restore the gas to its first condition, wherein the primary gas conditioning system includes flowing the gas at a first flow rate over a heating unit to increase the temperature of the gas and flowing the gas through a dehumidification unit at a second flow rate to reduce the relative humidity, wherein the first flow rate is slower than the second flow rate, and
recirculating the gas into the primary gas circulation loop;

providing one or more secondary gas circulation loop, wherein the secondary gas circulation loop comprises:
taking the gas in the envelope from a location spaced from the first end and the second end of the envelope at a third condition, wherein gas in the third condition has a lower temperature, higher relative humidity and/or reduced flow rate, relative to the first condition,
passing it through a secondary gas conditioning system to condition it to a fourth condition, wherein gas in the fourth condition has a higher temperature, lower relative humidity and/or a different flow rate, relative to the third condition, and
flowing the gas after conditioning to the fourth condition over at least another surface of the precast object; and
curing the precast object for a time sufficient to produce a cured precast object.

2. The process of claim 1 , wherein the precast object is made of a carbonatable calcium silicate-based cement and the gas is carbon dioxide.

3. The process of claim 1 , wherein at least one of the secondary gas conditioning system of the secondary gas circulation loop is located within the envelope.

4. The process of claim 2 , comprising providing a plurality of secondary gas circulation loops.

5. The process of claim 1 , wherein the secondary gas conditioning system comprises at least a heating unit to raise the temperature of the gas.

6. The process of claim 5 , wherein the secondary gas circulation loop comprises at least a fan to increase the flow of the gas.

7. The process of claim 6 , wherein the secondary gas circulation loop comprises a plurality of fans to increase the flow of the gas.

8. The process of claim 7 , wherein the secondary gas circulation loop has at least some of the fans configured to flow the gas in an opposite direction as compared with the other fans.

9. The process of claim 8 , wherein the secondary gas circulation loop has at least some of the fans configured to flow the gas at a first speed while the other fans as configured to flow gas at a speed different from the first speed.

10. The process of claim 6 , wherein the secondary gas conditioning system comprises a dehumidification unit to remove moisture from the gas and to reduce the relative humidity.

11. The process of claim 10 , wherein the dehumidification unit comprises a chiller, a desiccant, a membrane capable of moisture removal, or a combination of two or more thereof.

12. The process of claim 1 , wherein the fourth condition of the gas is substantially the same as the first condition of the gas.

13. The process of claim 1 , wherein the fourth condition of the gas is substantially different from the first condition of the gas.

14. The process of claim 1 , wherein the gas at the fourth condition after passing through the secondary gas conditioning system is flowed over the another surface of the precast object, wherein the another surface of the precast object is adjacent to the point where it was taken from within the envelope for passing through the secondary gas conditioning system.

15. The process of claim 1 , wherein the gas at the fourth condition after passing through the secondary gas conditioning system is flowed over the another surface of the precast object, wherein, the another surface of the precast object is at a point away from the point where it was taken from within the envelope for passing through the secondary gas conditioning system.

16. The process of claim 1 , wherein the precast object is a plurality of objects selected from the group consisting of pavers, blocks, roof tiles and railroad ties.

17. The process of claim 1 , wherein the precast object is a hollow core slab comprising a plurality of channels running along the length of the hollow core slab.

18. The process of claim 17 , wherein the hollow core slab comprises from about 4 to about 10 channels.

19. The process of claim 17 , wherein the gas at the first condition is introduced into the envelope through the channels of the hollow core slab.

20. The process of claim 17 , wherein the gas at the first condition is introduced into the envelope from the top or sides of the hollow core slab.

21. The process of claim 17 , wherein the gas at the first condition is introduced into the envelope from the bottom of the slab through the casting bed.

22. The process of claim 1 , wherein the first condition is characterized by a temperature of the gas, wherein the temperature of the gas is between about 20° C. to about 99° C.; and/or by the relative humidity of the gas, wherein the relative humidity of the gas is between about 0.1% to about 99%; and/or by the flow rate of the gas, wherein the flow rate facilitates an evaporation rate between about 1 kg/hr/mton to about 100 kg/hr/mton.

23. The process of claim 22 , wherein the second condition is characterized by a temperature of the gas, wherein the temperature of the gas is between about 20° C. to about 99° C.; and/or by the relative humidity of the gas, wherein the relative humidity of the gas is between about 0.1% to about 99%; and/or by the flow rate of the gas, wherein the flow rate facilitates an evaporation rate between about 1 kg/hr/mton to about 100 kg/hr/mton.

24. The process of claim 23 , wherein the third condition is characterized by a temperature of the gas, wherein the temperature of the gas is between about 20° C. to about 99° C.; and/or by the relative humidity of the gas, wherein the relative humidity of the gas is between about 0.1% to about 99%; and/or by the flow rate of the gas, wherein the flow rate facilitates an evaporation rate between about 1 kg/hr/mton to about 100 kg/hr/mton.

25. The process of claim 24 , wherein the fourth condition is characterized by a temperature of the gas, wherein the temperature of the gas is between about 20° C. to about 99° C.; and/or by the relative humidity of the gas, wherein the relative humidity of the gas is between about 0.1% to about 99%; and/or by the flow rate of the gas, wherein the flow rate facilitates an evaporation rate between about 1 kg/hr/mton to about 100 kg/hr/mton.

26. The process of claim 1 , wherein the primary gas conditioning system is configured such that the heating unit and the dehumidifying unit are arranged in parallel.

Assignees

• Solidia Technologies Inc

Inventors

• Jimenez Andrea Cecilia Montoya
• Atakan Vahit
• Martiny Andres
• Perry George Matthew
• Smith Kenneth Michael
• Patten Devin
• Castoro Daniel
• Narine Shalendra
• Seth Anuj
• Quinn Sean Camron

Classifications

• C04B2111/00019

  Carbon dioxide sequestration · CPC title

• C04B22/103

  Acids; Carbonic acids, e.g. from carbon dioxide · CPC title

• C04B20/0232

  with carbon dioxide · CPC title

• C04B40/0231 Primary

  Carbon dioxide hardening · CPC title

• Y02P40/18

  Carbon capture and storage [CCS] · CPC title