Advanced curing equipment and methods of using same

Patent metadata

Field	Value
Publication number	US-2018194693-A1
Application number	US-201715716392-A
Country	US
Kind code	A1
Filing date	Sep 26, 2017
Priority date	Jan 22, 2014
Publication date	Jul 12, 2018
Grant date	—

Abstract

Apparatus and methods for improving the curing process of materials that cure under reaction with CO 2 and that do not cure in the presence of water alone are described, and examples are given.

First claim

1 . An apparatus for curing materials that cure under reaction with CO 2 , comprising:
a curing chamber configured to contain a material that consumes CO 2 as a reagent, said material does not cure in the absence of CO 2 during curing, said material does not cure in the presence of water alone, and said material does not consume water during curing, said curing chamber having at least one port configured to allow said material to be introduced into said curing chamber and to be removed from said curing chamber, and having at least one closure for said port, said closure configured to provide an atmospheric seal when closed so as to prevent contamination of a gas present in said curing chamber by gas outside said curing chamber; a source of carbon dioxide or air configured to provide gaseous carbon dioxide or air to said curing chamber by way of a gas entry port in said curing chamber, said source of carbon dioxide or air having at least one flow regulation device configured to control a flow rate of said gaseous carbon dioxide or air into said curing chamber; a gas flow subsystem configured to circulate said gaseous carbon dioxide or air through said curing chamber; a temperature control subsystem configured to control a temperature of said gas within said chamber; a humidity control subsystem configured to control a humidity in said gas within said chamber; and at least one controller in communication with at least one of said source of carbon dioxide, said gas flow subsystem, said temperature control subsystem, and said humidity control subsystem,
said at least one controller configured to control independently at least a respective one of said flow rate of said gas inside the chamber, said circulation of said gas through said curing chamber, said temperature of said gas, and said humidity in said gas,
said at least one controller configured to provide a time of residence in a first drying phase (Phase 1), wherein a residence time in said first drying phase is configured to be minimized, and said at least one controller is configured to transition from said first drying phase (Phase 1) to a second carbonation phase (Phase 2) at the end of said first drying phase (Phase 1).

2 . The apparatus of claim 1 , wherein the apparatus is configured to first expose the material to the first drying phase (Phase 1) in absence of deliberately added CO 2 .

3 . The apparatus of claim 1 , wherein the apparatus is configured to first expose the material to the first drying phase (Phase 1) in presence of CO 2 .

4 . The apparatus of claim 1 , wherein the apparatus is configured to detect a transition from the first drying phase (Phase 1) to the second carbonation phase (Phase 2) by detecting a change in one or more electrical properties of the material on the surface or in the bulk thereof.

5 . The apparatus of claim 4 , wherein the one or multiple electrical properties of the material include at least one of a surface resistivity, a volume resistivity, a conductivity, an impedance, a capacitance, a dielectric constant, a dielectric strength, a permittivity, a piezoelectric constant, and a Seebeck coefficient.

6 . The apparatus of claim 1 , wherein the apparatus is configured to detect the transition from the first drying phase (Phase 1) to the second carbonation phase (Phase 2) by detecting a change in the quantity of water that is removed from the material.

7 . (canceled)

8 . (canceled)

9 . The apparatus of claim 1 , wherein the apparatus is configured to detect the transition from the first drying phase (Phase 1) to the second carbonation phase (Phase 2) by detecting a change in at least one of a CO 2 concentration and an O 2 concentration in the gas circulating in the chamber.

10 . (canceled)

11 . (canceled)

12 . The apparatus of claim 1 , wherein the apparatus is configured to detect the transition from the first drying phase (Phase 1) to the second carbonation phase (Phase 2) by detecting a change in temperature of the material.

13 . (canceled)

14 . (canceled)

15 . The apparatus of claim 1 , wherein the apparatus is configured to measure, track and control the pressure inside the chamber throughout the process in any of the first drying phase (Phase 1) and the second curing phase (Phase 2).

16 . The apparatus of claim 1 , wherein the apparatus is configured to detect the transition from the first drying phase (Phase 1) to the second carbonation phase (Phase 2) by detecting a change in the pH of the material.

17 . (canceled)

18 . (canceled)

19 . (canceled)

20 . (canceled)

21 . The apparatus of claim 1 , wherein the temperature control subsystem further comprises at least one energy source configured to heat at least one of the gas and the material.

22 . (canceled)

23 . The apparatus of claim 21 , wherein the energy source is configured to control the time of residence in at least one of the first drying phase (Phase 1) and the second carbonation phase (Phase 2).

24 . The apparatus of claim 21 , wherein said energy source is configured to employ fossil fuel combustion.

25 . The apparatus of claim 21 , wherein said energy source is configured to employ electrical resistance heating.

26 . (canceled)

27 . (canceled)

28 . The apparatus of claim 21 , wherein said energy source is configured to employ dielectric heating.

29 . (canceled)

30 . (canceled)

31 . (canceled)

32 . (canceled)

33 . (canceled)

34 . (canceled)

35 . (canceled)

36 . The apparatus of claim 21 , wherein said energy source is configured to employ a radiation heat source.

37 . (canceled)

38 . The apparatus of claim 1 , wherein the humidity control subsystem is configured to control the water extraction from the material.

39 . (canceled)

40 . (canceled)

41 . (canceled)

42 . (canceled)

43 . The apparatus of claim 38 , wherein the humidity control subsystem is configured to control the water extraction using a desiccant.

44 . The apparatus of claim 38 , wherein the humidity control subsystem is configured to control the water extraction using one of a heat exchanger and a chiller.

45 . (canceled)

46 . The apparatus of claim 1 , wherein the gas flow subsystem is configured to control the circulation of the gas in the chamber to control the water removal in the first drying phase (Phase 1) and to control the rate of reaction in the second carbonation phase (Phase 2).

47 . (canceled)

48 . The apparatus of claim 1 , wherein the gas flow subsystem is configured to control a flow and a velocity of the gas adjacent to the material.

49 . (canceled)

50 . (canceled)

51 . (canceled)

52 . The apparatus of claim 1 , wherein the gas flow subsystem is configured to control the flow and velocity of the gas using an external circulation system.

53 . (canceled)

54 . (canceled)

55 . (canceled)

5

Assignees

• Solidia Technologies Inc

Inventors

• Quinn Sean Camron
• Smith Kenneth Michael
• Patten Devin M
• Hu Xudong
• Perry George
• Atakan Vahit
• Jain Jitendra
• Seth Anuj
• Tas Ahmet Cuneyt
• Blacklock Alan Thomas
• Schuler Thomas
• Grootenboer Christopher J
• Castoro Dan

Classifications

• C04B40/0231 Primary

  Carbon dioxide hardening · CPC title

• B01J19/0033

  Optimalisation processes, i.e. processes with adaptive control systems (adaptive control systems per se G05B13/00) · CPC title

• B01J2219/00164

  controlling the flow · CPC title

• B01J19/0013

  Controlling the temperature of the process · CPC title

• B01J2219/00051

  Controlling the temperature · CPC title