CO2 IMPREGNATED CONCRETE

Abstract

Concrete made using the protocol described herein converts more of the available calcium hydroxide (Ca(OH).sub.2) into calcium carbonate (CaCO.sub.3) and distributes it more thoroughly throughout the concrete mixture by converting it into calcium bicarbonate (Ca(HCO.sub.3).sub.2) by adjusting the pH of the hydrating liquid and then deliberately adjusting the pH of the hydrating liquid again when precipitation of the CaCO.sub.3 from the hydration liquid is desired to more uniformly coat the materials used in a concrete mix. This process creates more CaCO.sub.3 in concrete than current methods on the market and that has been demonstrated to increase the structural and chemical properties of the concrete.

Claims

1. A method of increasing the strength and integrity of concrete, comprising: adding a high-surface-area polymer to a hydrating mixture of concrete; and allowing the high-surface-area polymer to integrate within a crystalline structure of the concrete.

2. The method of claim 1, wherein the high-surface-area polymer is polyethylene terephthalate (PET).

3. A method of increasing the strength and integrity of concrete, comprising: adding calcium carbonate (CaCO3) to an aqueous mixture of concrete; and allowing the mixture to set.

4. The method of claim 3, wherein the CaCO.sub.3 is generated from calcium hydroxide (Ca(OH).sub.2) in the hydrating mixture of concrete.

5. The method of claim 3, wherein the CaCO.sub.3 is precipitated onto surfaces of the concrete materials, for example aggregate, sand, and high-surface-area polymer during the hydration process

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0011] The disclosure, in accordance with one or more various embodiments, is described in detail with reference to the following figures. The drawings are provided for purposes of illustration only and merely depict exemplary embodiments of the disclosure. These drawings are provided to facilitate the reader's understanding of the disclosure and should not be considered limiting of the breadth, scope, or applicability of the disclosure. It should be noted that for clarity and ease of illustration these drawings are not necessarily made to scale.

[0012] FIG. 1 illustrates alite (Ca.sub.3SiO.sub.5) a component of portland cement;

[0013] FIG. 2 illustrates belite (Ca.sub.2SiO.sub.4) another component of portland cement;

[0014] FIG. 3 illustrates some of the chemical components of cement;

[0015] FIG. 4 illustrates some of the chemical shorthand used in concrete industry;

[0016] FIG. 5 illustrates carbonic acid, bicarbonate and carbonate equilibrium at different pH levels;

[0017] FIG. 6 illustrates various calcium carbonate crystalline structures;

[0018] FIG. 7A illustrates no connection between the PET plastic and concrete crystalline structure;

[0019] FIG. 7B illustrates no connection between the PET plastic and concrete crystalline structure;

[0020] FIG. 8 illustrates the embedment of micelles in CaCO.sub.3;

[0021] FIG. 9 illustrates electron microscopic images of micelle encapsulation;

[0022] FIG. 10 illustrates global PET plastic production capacity;

[0023] FIG. 11 illustrates plastic waste usage in U.S. tons;

[0024] FIG. 12 illustrates an embodiment of the compressive strength of portland cement with PAC aggregate replacement with smooth surfaced PET plastic;

[0025] FIG. 13 illustrates an embodiment of the concrete mixing process flow;

[0026] FIG. 14 illustrates details for Hopper 5 as shown in FIG. 13;

[0027] FIG. 15 illustrates details for Hopper 5 in FIG. 13, 4th embodiment; and

[0028] FIG. 16 illustrates an embodiment of an air lift material coating system.

DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS

[0029] The following description is presented to enable a person of ordinary skill in the art to make and use embodiments described herein. Descriptions of specific devices, techniques, and applications are provided only as examples. Various modifications to the examples described herein will be readily apparent to those of ordinary skill in the art, and the general principles defined herein may be applied to other examples and applications without departing from the spirit and scope of the disclosure. Thus, the disclosure is not intended to be limited to the examples described herein and shown but is to be accorded the scope consistent with the claims.

[0030] The word “exemplary” is used herein to mean “serving as an example illustration.” Any aspect or design described herein as “exemplary” is not necessarily to be construed as preferred or advantageous over other aspects or designs.

[0031] Reference will now be made in detail to aspects of the subject technology, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to like elements throughout.

[0032] The specific order or hierarchy of steps in the process disclosed herein is an example of exemplary approaches. Based upon design preferences, it is understood that the specific order or hierarchy of steps in the processes can be rearranged while remaining within the scope of the disclosure. Any accompanying method claims present elements of the various steps in a sample order and are not meant to be limited to the specific order or hierarchy presented.

[0033] Although the terms cement and concrete are often used interchangeably, cement is actually an ingredient of concrete. Concrete is basically a mixture of aggregates and paste. The aggregates are sand and gravel or crushed stone; the paste is water and portland cement. Concrete gets stronger as it gets older. Portland cement is not a brand name, but the generic term for the type of cement used in virtually all concrete, just as stainless is a type of steel and sterling a type of silver. Concrete normally comprises from 10 to 15 percent of the cement mix, by volume. Through a process called hydration, the cement and water harden and bind the aggregates into a rock-like mass. This hardening process continues for years meaning that concrete gets stronger as it gets older.

[0034] The manufacturing of portland cement—the material that provides most of the crystallization for concrete—is a complex process that involves mining and grinding raw materials that include limestone and clay to a fine powder and heating them to as high as 1,450° C. Unfortunately, this process is quite carbon positive; as of 2018, cement production contributed about 10% of all carbon emissions to the atmosphere.

[0035] This pollution comes from two sources: (a) the heating process, which is typically driven by combustion of hydrocarbons, creates environmental pollutants, including nitrogen oxides (NOx) and carbon dioxide (CO.sub.2); and (b) additional CO.sub.2 is released to the atmosphere during the chemical reaction at that elevated temperature. This reformation (sintering) of the limestone (calcium carbonate), when it is converted into calcium oxide (CaO) is what is known as a calcination reaction, described in Equation 1.

CaCO.sub.3.fwdarw.CaO+CO.sub.2  [1]

[0036] The cement preparation process can be made much greener using other patent pending technology by Robert Richardson (Provisional Patent Application No. 62/797,468 titled “CHEMISTRY SEQUESTERING OF CO2 USING CLOSED LITHIUM TECHNOLOGY,” filed 28 Jan. 2019; U.S patent application Ser. No. 16/773,293 titled “CHEMICAL SEQUESTERING OF CO2, NOx AND SO2”, filed 20 Jan. 2020; and International application PCT/US2020/015207 of the same name and filing date.) that has the propensity to capture point sources of CO.sub.2 made by combustion sources, for example cement kilns, and convert it in a carbon neutral or carbon negative way into sodium carbonate and sodium bicarbonate byproducts. The commercially viable byproducts of just referenced patent pending process by Richardson can be used as the source for CO.sub.2 as described herein. The carbonate and bicarbonate byproducts also have the propensity to reverse ocean acidification when responsibly dosed into the sea.

[0037] The CaO described in Equation 1 is not stable. If not reacted with silicon dioxide (SiO.sub.2) in the calcination process that results in cement, it will react with CO.sub.2 in the air to recreate CaCO.sub.3 in the reverse of Equation 1. Or, if exposed to H.sub.2O, it will form Ca(OH).sub.2, described in Equation 2.

CaO+H.sub.2O.fwdarw.Ca(OH).sub.2  [2]

[0038] During the calcination, CaO mineralizes with silicon dioxide (SiO.sub.2) to form two of the primary components of cement: alite, also known as tricalcium silicate (Ca.sub.3SiO.sub.5) and abbreviated as C.sub.3S in the concrete industry; and belite, also known as dicalcium silicate (Ca.sub.2SiO.sub.4) and abbreviated as C2S in the concrete industry. As the material temperature rises in the calcination process, belite is first to form. Then, with further temperature increase, some of the belite combines with additional CaO in the mixture to form alite. The elevated temperature also causes the material to begin melting and form nodules called “clinker”. Once clinker forms, the calcination process is complete, and the material is cooled. The rate of cooling affects the final ratio of alite and belite.

[0039] Once cool, the clinker is ground and mixed with mineral additives, including gypsum (CaSO.sub.4-2H.sub.2O), that influence the chemical processes that occur at a later time when this final cement product is hydrated for use in making concrete.

[0040] Alite is the major phase in portland cement responsible for setting and development of “early” strength. The other silicate, belite, contributes “late” strength, due to its lower reactivity. Alite is more reactive because of its higher calcium content and the presence of oxide ions in the lattice. FIG. 1 depicts the structure of alite. FIG. 2 depicts the structure of belite. Graphics for figures are from a Wikipedia article on alite and belite.

[0041] During the conventional cement hydration process the alite, belite and additives mix with water to form more than 30 crystalline products collectively known as Calcium Silicate Hydrates (C—S—H). The molecular formula abbreviations for the structure's components are connected with dashes to indicate there is no specific ratio relationship between the components of the mixture. The C—S—H structures have varying molecular ratios and include numerous impurities. Despite extensive investigation, this group's structural details are still poorly understood and yet concrete is one of the most used building materials in the world.

[0042] Although the ratios for C—S—H vary, the concrete industry has established generalized guidelines for the components. These are described in FIG. 3.

[0043] The “shorthand names” shown in FIG. 3 are based on the chemical abbreviations developed by the concrete industry. This shorthand is further explained in FIG. 4.

[0044] During a conventional concrete hydration process that begins when water is added to the mix of cement, sand, aggregate and possibly other additives, the crystallization that provides concrete strength is produced by the conversion of alite and belite in the cement into the C—S—H blend and calcium hydroxide (Ca(OH).sub.2), also known as CA. The abundance of Ca(OH).sub.2 in the hydrated cement paste varies with the ratio of H.sub.2O to cement and can reach approximately 26% of the total volume of a mature paste. Contrary to the C—S—H gel that is an ill-crystallized phase, Ca(OH).sub.2 is present predominantly in the form of well-defined crystalline structure (J. Marchand et al, Influence of Calcium Hydroxide Dissolution on the Transport Properties of Hydrated Cement Systems—Laval University, Canada 2021).

Description Process

[0045] Concrete made using the protocol described in this document converts more of the available Ca(OH).sub.2 into calcium carbonate (CaCO.sub.3) and distributes it more thoroughly throughout the concrete mixture by a process that solarizes CaCO.sub.3 as calcium bicarbonate (Ca(HCO.sub.3).sub.2) and then precipitates it again onto materials in the concrete mix as CaCO.sub.3 when the pH of the hydration water is changed by the unique concrete mixing environment provided in this process/protocol. This process/protocol is subsequently described in detail.

[0046] The addition of CO.sub.2 to a confined environment around the concrete hydration process of this protocol is important because the CO.sub.2 gas in the atmosphere dissolves into the water used to hydrate cement, often replenishing consumed CO.sub.2 in the hydrate. A portion of the dissolved CO.sub.2 spontaneously converts to carbonic acid (H.sub.2CO.sub.3) and the H.sub.2CO.sub.3 reacts with the Ca(OH).sub.2 and other materials in the concrete mix to produce calcium carbonate (CaCO.sub.3) and other crystallin structures. Some of these reactions are shown in Equations 3,4 & 5.

[0047] The concrete hydration process described herein, that occurs in an enclosed environment with elevated CO.sub.2 gas and uses water with dissolved CO.sub.2 and minerals, has demonstrated the ability to enhance the production of calcium carbonate (CaCO.sub.3) and other compounds that form interconnected crystals in the concrete, resulting in a final product with increased structural and chemical resistance characteristics. This is explained in greater detail later.

[0048] The Ca(OH).sub.2 in cement is not a stable compound. It reacts with CO.sub.2 to form CaCO.sub.3 according to Equation 3. In conventional concrete production, this reaction can use CO.sub.2 from the atmosphere but there may not be enough CO2 available during mixing to react with all of the Ca(OH)2 present in the cement. The process described herein fully converts the Ca(OH).sub.2 to CaCO.sub.3 because the concrete mixing is done in an environment that provides the required amount of CO.sub.2. The CO.sub.2 is supplied to the concrete mix in the water used for hydration and provided in the atmosphere of the container used for cement mixing.

[0049] Furthermore, the process described herein regulates the concentration of CO.sub.2 in the hydration water, and the hydration water pH, and the concentration of CO.sub.2 in the gas in the atmosphere of the mixing environment. All of these variables are coordinated in a way that optimizes the placement of CaCO.sub.3 and other materials on surfaces of aggregate and other components in the concrete mix in a way that optimizes the final product strength and chemical characteristics.

Ca(OH).sub.2+CO.sub.2.fwdarw.CaCO.sub.3↓+H.sub.2O(ΔH.sup.0.sub.298=−108.40 kJ)  [3]

CO.sub.2+H.sub.2O.fwdarw.H.sub.2CO.sub.3  [4]

H.sub.2CO.sub.3+CaCo.sub.3.fwdarw.Ca(HCO.sub.3).sub.2tm [5]

[0050] The pH of the hydration water is regulated through addition of carbonates, bicarbonates, oxides, and acids, for example carbonic acid, to affect the placement of CaCO.sub.3 and other minerals. FIG. 5 graphically shows how a change in the pH determines which of the three reactions shown in Equations 3, 4, and 5 will occur in the concrete mix. Part of the technology described in this document pertains to the adroit regulation of these processes and others through the regulation of the mix pH, to enhance concrete strength and reduce permeability.

[0051] A brief introduction to the significance of the chemical equilibrium described in FIG. 5 is provided to contribute understanding of how pH adjustment in the concrete mix facilitates the creation of reaction environments that selectively favor Equations 3-5. The technology described in this document introduces two methodologies not found in conventional mixing procedures for portland cement-based concrete: the pH adjustment of water used for hydration in the concrete mix, and the addition of CO.sub.2 gas into the concrete by mixing the concrete in an enclosed CO.sub.2 enriched environment. The water pH is adjusted through a controlled chemical reaction with adjustment to the amount of CO.sub.2 gas in the atmosphere of the enclosed mixing environment and through the dissolved carbonate and bicarbonate and hydroxide compounds previously added into the hydration water, for example, calcium bicarbonate and calcium hydroxide.

[0052] The addition of precisely dosed amounts of CO.sub.2, bicarbonate, carbonate, hydroxide can create a liquid pH at a designated value anywhere between an acidic value of 3.6 and a basic value of 11.6. The solution pH determines which of the following forms will express themselves: H.sub.2CO.sub.3 HCO.sub.3.sup.−CO.sub.3.sup.2−. When the liquid in the concrete mix has a pH below 6, the H.sub.2CO.sub.3 is the predominant component of the carbonate mix. The HCO.sub.3.sup.− ion is the predominant carbonate component at a liquid pH between 7 and 10, and CO.sub.3.sup.2− is the predominant carbonate component when the liquid pH is above 11.

[0053] Therefore, Equation 3 is prevalent in a liquid with pH above 11, Equation 4 is prevalent at a liquid pH between 2 and 6, and Equation 5 is prevalent in a pH range between 7 and 10.

[0054] When the pH-specific water is added to the concrete mix it will react with its environment in accordance with its pH. The reactions between the water and the concrete mix will adjust the water pH and limit the extent to which a desired reaction will continue. However, this technology allows reactions described in Equations 4 and 5 to continue by re-introducing CO.sub.2 into the water from the CO2 gas in the mixing environment. The amount of CO.sub.2 in the concrete mixing environment is precisely metered to effect the desired reaction within the mix. Details of how this is accomplished is provided later in this document.

[0055] Research by Jiang et al (Jiang, Calcite crystallization in the cement system: morphological diversity, growth mechanism and shape evolution—Phys. Chem. Chem. Phys., 2018), reexamined the phenomenon of carbonation in a cement system from the micron to nanometer scale. The research included calcium carbonate formation from lab-made C—S—H exposed to atmospheric CO.sub.2 (approximately 420 ppm) at 25° C. and 50% relative humidity. Two crystal shapes were formed: cubic and spindle, as shown in FIG. 6. The study's conclusion identified a reaction between CO.sub.2 and Ca(OH).sub.2—Equation 3, as the main source for crystalline CaCO.sub.3 in portland cement. Similar results are found in literature (Cui, et al, Cem. Concr. Compose., 2017,77, 81-85).

[0056] The field of “concrete additives” is broad and complicated with many cross interactions between possible compound combinations. This document acknowledges that some concrete additives or additive combinations will germanely influence the chemistry and process described herein. Therefore, this document cautions against the addition of additives other than those specifically identified herein to a concrete mix when the results of the technology described in this document are desired.

[0057] Aspect 1—The Redistribution of CaCO.sub.3

[0058] The first aspect of the process described in this paper focuses on rebalancing CaCO.sub.3 within the concrete mixture to enhance product strength and reduce porosity. Through the use of pH adjustment in the process described below, CaCO.sub.3 can be made from Ca(OH).sub.2 or re-dissolved from an area within the concrete mix—for example, deposits of CaCO.sub.3 formed from Ca(OH).sub.2 that can comprise up to 26% of the mix mass in portland cement , and during, concrete hydration, by transporting and re-distributing the CaCO.sub.3 in the hydration water after it is converted to soluble Ca(HCO.sub.3).sub.2. The Ca(HCO.sub.3).sub.2 is re-deposited as CaCO.sub.3 again on another surface within the concrete mixture when the pH of the hydration water is subsequently changed. The re-depositing occurs when the water pH is increased through its exposure to the minerals in the concrete mix or adjustments in the water pH through the reduction of gas phase CO.sub.2. This is an important feature of this process because it allows a more uniform distribution of CaCO.sub.3 within the mixture and that is positively related to increased concrete physical properties, for example compressive strength.

[0059] In the first embodiment of this process, the concrete mixture contains conventional aggregate and no high-surface-area PET or other polymer. In this embodiment, the CaCO.sub.3 is redistributed throughout the mix, and that provides three benefits: (a) more consistent bonds between aggregate and sand to C—S—H and other crystalline structures within the concrete mixture; and (b) it reduces the number of holes in the overall concrete crystalline structure, which reduces opportunities for internal attack from chemicals and general degradation through permeation; and (c) the concrete tensile and compressive strength of the concrete product are increased.

[0060] In the second embodiment of this process, the concrete mixture contains a both conventional aggregate and high-surface-area PET or another polymer. In this embodiment, the CaCO.sub.3 is redistributed throughout the mix and provides five benefits: (a) more consistent bond aggregate and sand to C—S—H and other crystalline structures within the concrete mixture; and (b) the encapsulation of high-surface-area PET or other polymer into the overall crystalline structure of the concrete; and (c) reduction in the number of cavities within the concrete; and (d) reduces the weight of the concrete because the polymers have lower density than stone aggregate; and (e) the concrete tensile and compressive strength of the concrete product are further increased in direct proportion to the amount of high-surface-area polymer added.

[0061] In the third embodiment of this process, the concrete mixture utilizes high-surface-area PET or other polymer(s) to provide structure and volume to the concrete mix in place of conventional aggregate. In this embodiment, the CaCO.sub.3 is redistributed throughout the mix to provide five benefits: (a) more consistently bonding to segments of C—S—H and other crystalline structures within the concrete mixture into a homogeneous material; (b) the encapsulation of high-surface-area PET or other polymer into the overall crystalline structure of the concrete; (c) reduction in the number of cavities in the concrete crystalline structure; (d) further reduction in the weight of the concrete per unit volume because the polymers are less dense than stone aggregate; and (e) the concrete tensile and compressive strength of the concrete product are further increased, beyond the increases from the second embodiment, in direct proportion to the amount of high-surface-area polymer added.

[0062] The basics of this process are summarized again for added clarity. This process creates, dissolves, and relocates CaCO3 within the concrete mix during the hydration process. Controlled variations in the pH of water used for hydration determines which of the three activities will occur. Specific structural and chemical characteristics of the concrete batch are achieved through a combination of two variables, the specific pH adjustment sequences of water use for hydration and controlled variations in the concentration of CO.sub.2 gas within the atmosphere of the enclosed space used for concrete hydration.

[0063] Optimized concrete physical properties are produced through repeated wetting and simultaneous dissolving or deposition of CaCO.sub.3 on the aggregate, sand, and other additives included in a batch of concrete by water used for hydration that is impregnated with CO.sub.2 and other additives. This process optimizes the CaCO.sub.3 crystal formation that integrates the components of the concrete mix into a monolithic structure. The add mixture enhancements to the water and atmosphere within the hydration chamber can be done manually or via an automated process.

[0064] The CO.sub.2 enhanced water converts CaCO.sub.3 in the concrete mix into aqueous Ca(HCO.sub.3).sub.2 solution according to Equations 4 & 5.

[0065] The aqueous Ca(HCO.sub.3).sub.2 solution interacts with minerals in the concrete mixture. For example: (a) the aqueous solution can hydrate dry mineral material, and that interaction can dissolve the previously dry minerals and include them in the aqueous solution. This process can influence the pH of the aqueous solution. One result of a pH change is the conversion of Ca(HCO.sub.3).sub.2 into CaCO.sub.3 with resulting precipitation of the CaCO.sub.3; and (b) the aqueous Ca(HCO.sub.3).sub.2 can interact with minerals in a way that results in dissolving a portion of the mineral material. The increased total dissolved solids level in the aqueous Ca(HCO.sub.3).sub.2 mix can push the CO.sub.2 past its solubility limit and cause it to be expelled from the liquid into the closed reaction environment. This expulsion can facilitate a reaction between the gas phase CO.sub.2 and Ca(OH).sub.2 in the concrete mix to produce CaCO.sub.3 as described in Equation 3. The gas-phase CO.sub.2 can also be re-dissolved into water in another area within the reaction chamber.

[0066] Aspect 2—The Creation of High-Surface-Area Polymers that are Effectively Integrated into Concrete Crystalline Structure.

[0067] A second aspect of this process is the strengthening of the concrete through the encapsulation of high-surface-area polymer or other material that contains nano to macro scale surface irregularities and protrusions into the concrete's crystalline CaCO.sub.3 and C—S—Hbinders.

[0068] Added concrete strength is developed through a strong crystalline connectedness produced between components of the concrete mix including conventional aggregate and/or polymer materials with nano to macro scale surface irregularities and protrusions. This occurs to some extent during the conventional concrete hydration process but is enhanced when the pH regulated hydration water containing carbonate and bicarbonate minerals is used in the concrete mixing process. The high-surface-area polymer described herein attaches to the CaCO.sub.3 and other crystallin structures within the concrete more effectively than conventional aggregate because of its increased high surface area exposed to the crystal attachment.

[0069] In some embodiments, the polymer material is made from previously used polymer materials (e.g., PET drinking water bottles). The previously used polymer or other polymer is re-engineered in a way to increase surface area and/or surface reactivity to enable coating and integration into the crystalline structure of the concrete.

[0070] This process is not related to the conventional use of low surface area polymers as primary plasticizers in concrete or the use of low surface area polymers merely as aggregate. In this process, the high surface area of added polymers allows it to be integrated directly into the crystalline structure of C—S—Hand CaCO.sub.3. Low surface area polymers have proven not to connect with the C—S—Hand CaCO3 as shown in FIGS. 7A & B.

[0071] FIGS. 7A & 7B prepared by Zoe Harmonie (Zoe Harmonie Lee, Modification of Waste Aggregate PET for Improving the Concrete Properties, Advances in Civil Engineering-Volume 2019, Article ID 6942052) clearly show no connection between the PET plastic and concrete crystalline structure. In preparation for his inclusion of PET plastic within the concrete mix the PET was treated with calcium chlorite (Ca(ClO.sub.2).sub.2 and hydrogen peroxide (H.sub.2O.sub.2) but this treatment did not produce the high surface area produced by the process described in this document. The high-surface-area process presented in this paper does prepare the PET (or other polymer) surface with nano scale fibrous structures and holes. The technology used to produce this accomplishment is described in greater detail below.

[0072] The use of high-surface-area fibers described in this document means polymer or other material that contains nano scale fibrous features that enable them to be encapsulated into the CaCO.sub.3 and C—S—Hcrystal structure. Without nano-micro scale surface irregularities and protrusions on the polymer, the CaCO.sub.3 and C—S—Hmaterials have no point of contact that is conducive to crystalline attachment and encapsulation.

[0073] The work by Jiang, et al, provided insight for the development of the polymer encapsulation methodology. Jiang observed micelles are tightly encapsulated during a CaCO.sub.3 crystallization process. Although micelles are not made of PET, they are representative because they both present a non-polar surface to the CaCO.sub.3 and other minerals that precipitate in the crystallization process during the concrete hydration process. The crystalline attachment between the micelles and CaCO.sub.3 and other minerals was tight enough to deform the soft micelles Jiang used in the experiments. This tight connection is required for the integration of a polymer into the overall concrete crystalline structure in a way that will effectively increase the overall monolith strength. FIG. 8 shows an artistic depiction of the micelle encapsulation process during Jiang's CaCO.sub.3 crystallization.

[0074] Explanation of FIG. 8. Micromechanical simulation of the initially spherical micelle [101] incorporation. During burial, lateral micelle compression is accompanied by an initial downward contraction followed by upward extension. The bottom dashed line [101] indicates the surface on which the micelle is initially attached, while the horizontal solid lines [102] represent the top surface of the crystal as it grows around the micelle. The dark part of the micelle outline [103] shows boundary between crystal and micelle. The dot at the top of the micelle [104] outline represents the highest point of the micelle deformation caused by encapsulation within the crystal.

[0075] The micelle capture process is shown in FIG. 9 uses electron microscopy to literally show the process described graphically in FIG. 8. Subsections (d) through (h) of the photographic assemblage best shows the process described graphically in FIG. 8. The red arrows in the FIG. 9 sequence d-h shows the process of micelle encapsulation within the CaCO.sub.3 crystalline structure.

[0076] The following is the explanation of FIG. 9 that accompanied the graphic in its original format. Incorporation of carboxylated micelles and associated cavity generation. (a-c). Sequential in situ 3×3 μm AFM images of growing calcite surface at σ=1.49. Particles indicated by arrows in image (a) subsequently show a decrease in height in image (b), before undergoing complete burial in image (c). The times at which the bottom and top of the images (a-c) were collected are given in lower and upper right corners of images respectfully. Images (d-h) provide a detailed view of the burial of a large micelle (σ=2.66) into the crystallin structure. Image (i) shows calcite surface with adsorbed micelles (green arrows).

[0077] Why is there a focus on reused PET as the polymer of choice for this process? First, it is abundant. The world production of PET in 2017 was 30.3 million tons. FIG. 10 shows the global production capacity for PET.

[0078] PET is manufactured in such large quantities because it is useful. The plastic is lightweight, water resistant, strong, non-toxic, and inexpensive (especially when recycled materials are used). Unfortunately, only about 29% is reused in some way, as shown on FIG. 11.

[0079] Fortunately, the process described in this document has the propensity to dramatically improve the percentage of reused PET.

[0080] PET's high production capacity is the result of its superior physical attributes. It is: readily available and relatively inexpensive; has high a strength-to-weight ratio; a tensile strength at yield of 85.5 MPa (concrete tensile is 2-5 MPa); a compressive strength at 2% deformation of 82.7 MPa (concrete compressive strength is 20-40 MPa); it is very resistant to moisture; has excellent chemical resistance to organic material and it is not biodegradable, which is good and bad, depending on your perspective on its intended use; it is virtually shatterproof; not toxic; and is easily recycled. These same attributes make PET a good choice for strength enhancement in concrete.

[0081] As noted above, smooth surfaced plastics are currently used in concrete as aggregate, but the process described in this paper takes exception to that process. In the process described in this document, only polymers or other materials with nano and micro irregularities and protrusions over all of its surface areas are integrated directly into the CaCO.sub.3 and C—S—H crystalline structure through encasement of their nano and micro irregularities and protrusion by crystal growth.

[0082] On the contrary, the current practice of using low surface area PET as an “aggregate” in lightweight concrete has lowered the tensile and compressive strengths of concrete when compared concrete that does not include smooth/low surface area PET in lightweight concrete. This is the case because the low surface area PET is not attached to the crystalline structure of the concrete.

[0083] The previous statement is corroborated by Casanova-del-Angel et al (Casanova-del-Angel, et al, Manufacturing Light Concrete with PET Aggregate, International Scholarly Research Network 2012) research that provided comprehensive comparison tests between portland cement with conventional limestone aggregate and portland cement with low surface area PET aggregate. The following is a summary of his work:

[0084] Cement consumption is higher for light concretes with PET than for natural portland concretes.

[0085] The water/cement ratio is lower for light concretes than natural portland concretes.

[0086] The tensile strength of light concretes (with low surface area PET) is between 77% -82% of natural portland concrete.

[0087] The compressive strength comparison at 28 days was 222.06 kg/cm.sup.2 for natural cement and 215.45 kg/cm.sup.2 for light (PET) concrete.

[0088] There is a higher consistency for light concrete mixtures that contain low surface area PET than for natural concrete mixtures.

[0089] Although not included in the summary by Casanova-del-Angel, it is clear to a person having ordinary skill in this art that the low surface area PET aggregate did not have the same irregular surface finish as the limestone aggregate used in the conventional portland concrete. There was no mention in the article of any conditioning of the low surface area PET surface, and, therefore, one must conclude that the PET aggregate had the smooth/low surface area conventionally found on the plastic. The limestone aggregate naturally has irregularities that provide higher surface area and points of attachment. Furthermore, low surface area PET is known to be hydrophobic and will therefore resist interaction with liquids in the concrete mix that contain suspended carbonate.

[0090] Additional research on the use of low surface area PET in concrete was conducted by Nursyamsi, et al. (Nursyamsi, et al, The influence of PET plastic waste gradations as coarse aggregate towards compressive strength of light concrete, University of Sumatera Utara, Jalan Perpustakaan No.5, Medan, 20155, Indonesia) His conclusion was that the surface area of PET with its shiny texture (glassy) made the attachment with concrete weak.

[0091] Research by Zoe Harmonie et al acknowledge the findings described above and referenced others that corroborate the understanding that untreated low surface area PET has a smooth and hydrophobic surface that prevents attachment or inclusion in calcium-based crystal structures inherent in portland concrete. His research did investigate the effects of treating low surface area PET waste using hydrogen peroxide (H.sub.2O) and calcium hypochlorite solution (Ca(ClO).sub.2) before incorporating it in concrete as a coarse aggregate replacement.

[0092] FIG. 12 reports Zoe Harmonie findings regarding decreased compressive strength with increased percent smooth/low surface area PET (identified as “PAC replacement” on the graph). It also shows that the low surface area PET treatment with H.sub.2O.sub.2 and Ca(ClO).sub.2 does make a modest improvement in the concrete compressive strength that is actually inconsequential in comparison to the overall decline in strength caused by the lack of attachment between the low surface area PET surface and the concrete crystalline structure.

[0093] The article by Zoe Harmonie includes photographs presented in FIG. 7A and 7B that explain to someone with ordinary skill in the art that there is no connection between the low surface area PET and the concrete crystalline structure.

[0094] The modest improvement in concrete strength shown in comparison between the low surface area PET treated with H.sub.2O.sub.2 and Ca(ClO).sub.2 and the untreated low surface area PET presumably depicts the elimination of surface hydrophobic characteristic of the low surface area PET. This treatment process also provides the same benefit to the high-surface-area polymers presented in this specification for the same reason.

[0095] The combination of high-surface-area created by added nano-scale surface perturbations and oxidation of polymer functional groups to increase hydrophilic attraction is an optimal combination. This combination improves the enhanced high-surface-area PET's receptivity for encapsulation described previously by Jiang.

[0096] Methodology for producing high-surface-area on polymers was developed from work done by Mohamed, et al (Mohamed et al, Porous Copolymer Resins: Tuning Pore Structure and Surface Area with Non-reactive Porogens, Nanomaterials (Basel). 2012 Jun; 2(2): 163-186). The polymer chemistry process Mohamed describes involving nonreactive porogen solvents is incorporated as step 4 in the overall high-surface-area preparation process described below.

[0097] Mohamed's work describes the technique of creating nano-size polymer structures by adding a porogen solvent to the polymerization process liquid. His paper describes the “art” of selecting a porogen solvent that is compatible with the reaction and other technical details. For example, the appropriate porogen solvent does not chemically react with the polymerization process; instead, it creates temporary physical obstacles that interfere with laminar crystallization and force the crystallization to build around them. In the process, the crystallization pattern is filled with nano to micro size perturbations. The generic description of perturbation methodology provided guidance that resulted in the development of the purpose-specific nano technology process used in this technology for the modification of existing polymers.

[0098] The nano filament high-surface-area process described in this document has 6 steps. I am deliberately omitting process details for protection as trade secrets.

[0099] Begin by partially dissolving the clean and chipped scrap low surface area PET. The dissolving can be done many ways; one that provided consistently good results will be used as an example. Degradation using heated dimethyl sulfoxide (DMSO) (C.sub.2H.sub.6OS) as a solvent and hydrotalcite (Mg.sub.6Al.sub.2CO.sub.3(OH).sub.16.Math.4H.sub.2O) as a catalyst. This method must be used with discretion because it has the ability to completely decompose low surface area PET in just a few minutes. Process temperature, stirring speed and use of catalyst are the primary controls on rate of reaction. The desired low surface area PET digestion percentage is between 5% and 25%, but there are situations when more or less are desirable. The determination of an optimized reaction condition including temperature, time and agitation was determined empirically and verified with electron microscopy.

[0100] Once the desired percent of low surface area PET disassembly is achieved, the reaction mixture is cooled. The addition of sodium hydroxide (NaOH) in methanol (CH.sub.3OH) to a cooled solution will precipitate the two PET monomers: dimethyl terephthalate DMT (C.sub.6H.sub.4(COOCH.sub.3).sub.2) and ethylene glycol EG (HOCH.sub.2CH.sub.2OH). The DMSO solvent and hydrotalcite catalyst can be used again after distillation, if desired.

[0101] The remaining (non-digested) low surface area PET is air dried at 190° C. to evaporate any remaining DMSO.

[0102] The dry and cool low surface area PET that was not digested is introduced to the DMT and EG monomers made during the PET' s partial disassembly with a catalyst like antimony oxide (Sb.sub.2O.sub.3) and a non-reactive porogen solvent. These are combined in a process called suspension polymerization. The porogen solvent does not interact with the new polymerization chemically, but it does become physically involved in the re-polymerization process by “interfering with uniform crystallization in ways that create tunable pore structures and other shapes” that create high polymer surface area. Success in this process is directly related to the selection of the porogen solvent. An inappropriate choice of porogen solvents will create polymer that contains large clusters that reduce the polymer surface area. When done correctly, the reformed-polymer can have a surface area with 10.sup.1 to 10.sup.3 m.sup.2/g. Some of the candidates for porogens in this example involving polymers associated with PET are toluene or cyclohexanone. Both were effective in my research, but the toluene seems to produce the most consistent results.

[0103] Once the PET high-surface-area polymerization is complete, the product is rinsed in H.sub.2O to remove residuals from the polymerization step and bathed with agitation in a calcium bicarbonate (Ca(HCO.sub.3).sub.2) solution at a pH between 7 and 10 for several hours or more. Agitation can be provided by turbulent liquid flow that causes the high-surface-area PET flakes to tumble in solution.

[0104] The high-surface-area PET is dried at completion of the calcium carbonate bath and packaged for use in Hopper 5 of the concrete production process described in this document and shown in FIG. 13.

[0105] The following is an example of the many possible ways the high-surface-area PET product made from the process described above could be implemented in concrete hydration. These descriptions reference equipment shown in FIG. 13.

[0106] The concrete production technology displayed in FIG. 13 can be used as a batch or continuous process. This discussion is intended to provide an understanding that applies to both options.

[0107] The adjustment of concrete hydration water pH, concentration of dissolved CO.sub.2 and the dosing rate of CO.sub.2 gas into the mixing chamber's headspace (atmosphere) can occur manually or via an automated program that gathers sensor data from the concrete batch and integrates it into electronic directives that regulate the CO.sub.2, carbonate, and bicarbonate dosing devices and the amount of all other materials added to the concrete mix. The automated methodology has the propensity to produce a concrete mix with more predictable results. In either case, this process requires dissolving CO.sub.2 into water, and dosing carbonates and/or bicarbonates into the concrete hydration water then dosing of CO.sub.2 into the closed concrete mixing reactor.

[0108] If the process control is manual, it is effected through manual positioning of hardware valves, hoppers etc. with minimal aid from instrumentation such as pH, temperature, total dissolved solids, and others.

[0109] If the mix is made using an automated program, the controller could be a PLC, FPGA, PC, Arduino, Raspberry Pi, or other type of programmable controller, hereinafter referred to as PLC. Data from process sensors such as pH, TDS, temperature, CO.sub.2, weight of raw materials, and others is processed through a program that includes if-then logic, algorithms, and other programming to produce electronic commands that operate mechanical devices such as valves, hoppers, mixers, and other devices.

[0110] A PLC provides the operator with an opportunity to enter the batch-specific specifications pertaining to desired product strength, slump, gel time, quantity, chemical resistance, site temperature at point of use, and more. The mix process is controlled in real time using sensor data integrated into a quality control program sequence within the PLC. The PLC provides local displays on Human Machine Interface (HMI) screens or equivalent, provides local alarms, the ability to integrate with a Local Area Network (LAN), and relays data to the equipment supplier via LAN, modem, or other means that is required to monitor equipment performance. A remote communication ability between the process control equipment and the equipment supplier can also be used to monitor error conditions to determine if maintenance is needed, download updated programs, provide information for re-ordering of consumable supplies, and program lock-out if royalties are not paid.

Batch Plant Operating Sequence

[0111] The process begins by generating and storing CO.sub.2 gas in Reaction Chamber A. The chamber is equipped with valves to regulate product flow in and out of the vessel, a pressure relief device, a pH probe, and an ability to mix the materials introduced into it. Hopper 1A stores a granular or liquid bicarbonate or carbonate material, for example sodium bicarbonate (NaHCO.sub.3), calcium bicarbonate (Ca(HCO.sub.3).sub.2 or sodium carbonate (Na.sub.2CO.sub.3). The hopper is pressurized to match the pressure of Chamber A and supplied with an automated valve and metered way to control the flow of product from the hopper into Reaction Chamber A. Metering can be accomplished many ways, for example, measuring the flow rate and flow time of material of known concentration leaving Hopper 1A, or measuring the difference in weight of Hopper 1A before, and after material has been transferred to Reaction Chamber A, or by transferring a quantity of material from Hopper lA into an intermediate container that can determine the weight or volume of material introduced into it prior to further transferring the material into Reaction Chamber A. In another embodiment, the weight of Reaction Chamber A is measured to determine the quantity of ingredients added and/or removed. In this embodiment, one or more load cells are incorporated into the supporting structure of the hoppers and or reaction chamber to measure weight/mass.

[0112] An acid of known concentration, for example hydrochloric acid (HCl) is stored in Hopper 2. The hopper is pressurized, or the HCl can be pumped into Reaction Chamber A. In either event, Hopper 2 is supplied with an automated valve to control the flow of product from the hopper and a way to meter the amount of product that is introduced into Reaction Chamber A. Metering can be accomplished many ways, for example measuring the flow rate and flow time of material of known concentration leaving Hopper 2, or measuring the difference in weight of Hopper 2 after material has been transferred to Reaction Chamber A, or by transferring a quantity of material from Hopper 2 into an intermediate container that can determine the weight or volume of material introduced into it prior to further transferring the material into Reaction Chamber A.

[0113] The production of CO.sub.2 gas in Reaction Chamber A is an automated or batch process. Alternatively, the CO.sub.2 can also be supplied to Reaction Chamber C as cylindered gas or liquid product supplied from another source. At the completion of a reaction or at a designated interval, spent products are discharged via a port on the bottom of Reaction Chamber A when a valve is opened. Gas pressure and gravity provide the incentive for spent liquid to move through an open valve into Vessel B. The discharge port can be fitted with sensors that detect liquid flow and trigger valve closing when the spent liquid has voided Reaction Chamber A.

[0114] The Equations 6-11 are examples of possible reactions to produce CO.sub.2 gas:

Na.sub.2CO.sub.3 (aq)+2 HCl (aq).fwdarw.2 NaCl (aq)+CO.sub.2(g)+H.sub.2O(1)  [6]

NaHCO.sub.3(aq)+HCl(aq).fwdarw.H.sub.2O(l)+CO.sub.2(g)+NaCl(aq)  [7]

Na.sub.2CO.sub.3(aq)2HNO.sub.3(aq).fwdarw.H.sub.2O(l)+CO.sub.2(g)+2NaNO.sub.3(aq)  [8]

NaHCO.sub.3(aq)+HNO.sub.3(aq).fwdarw.H.sub.2O(l)+CO.sub.2(g)+NaNO.sub.3(aq)  [9]

Ca(HCO.sub.3).sub.2(aq)+2HCl(aq).fwdarw.caCl.sub.2(aq)2CO.sub.2(g)+2H.sub.2O(l)  [10]

ca(HCO.sub.3).sub.2(aq_+2HNO.sub.3(aq).fwdarw.Ca(NO.sub.3.sub.2(aq)+2CO.sub.2(g)+2H.sub.2O(l)  [11]

[0115] All of the reactions produce products that have commercial value. The NaCl produced in Equation 6 and 7 can be used as the consumable for a separately patented process by Robert

[0116] Richardson that was reference earlier in this document that captures CO.sub.2 and converts it into sodium bicarbonate (NaHCO.sub.3) and sodium carbonate (Na.sub.2CO.sub.3). This invention can be used to generate the Na.sub.2CO.sub.3 and NaHCO3 for the process described in this document. The NaNO3 produced in Equations 8, 9 & 11 can be used as a fertilizer for plants and crops.

[0117] The equipment described in this section can make concrete in batch mode or continuously. The PLC has programs for both options. Each option is further refined during use by information from sensors affixed to process equipment. The following description provides generic orientation to the variables monitored and the influence each additive contributes to the overall concrete mixture.

[0118] Hopper 3 is filled with H.sub.2O at chilled or ambient temperature. Cooler water will dissolve more CO.sub.2 than warm or hot water. The hopper can include water chilling apparatus and sensor(s) for pH, for temperature, and for Total Dissolved Solids (TDS). Other sensors for water mineral content can also be added. The information from sensors is relayed to the process controller for determination of the H.sub.2O quantity necessary for the calculated batch or continuous production mode.

[0119] Hopper 3 is supplied with an automated valve and pump to transfer the H.sub.2O into Reaction Chamber C. Metering can be accomplished many ways, for example measuring the flow rate and flow time of material leaving Hopper 3, or measuring the weight of Hopper 3 before and after material has been transferred to Reaction Chamber C, or by transferring a quantity of material from Hopper 3 into an intermediate container that can determine the weight or volume of material introduced into it prior to further transferring the material into Reaction Chamber C.

[0120] Reaction Chamber C can produce enhanced water for many different concrete mixes and applications. For example, a unique hydration liquid formula can be made for each type of concrete the plant can make, each with different physical characteristics, and/or the plant can create mixtures for pre-treating aggregate or high-surface-area polymers.

[0121] If a facility requires different carbonated water and mineral mixes at the same time, then at least two copies of Reaction Chamber C (FIG. 13) will be required. Each copy will ideally have one Hopper 3 and one or more Hopper 1B's.

[0122] When more than one Reaction Chamber C is required, it is recommended that both be equipped identically despite the separate planned usage. This feature provides redundancy and flexibility of the equipment's application. The units are equipped with valves to regulate product flow in and out of the vessel, a pressure relief device, a pH probe, TDS probe, temperature probe, CO.sub.2 concentration, and an ability to mix the materials introduced into it.

[0123] One or more Hopper 1B devices store a granular or liquid bicarbonate material or other concrete add mixtures, for example sodium bicarbonate (NaHCO.sub.3) or calcium bicarbonate (Ca(HCO.sub.3).sub.2) or sodium carbonate (Na.sub.2CO.sub.3). The hopper is supplied with a valve and pump to control the flow of product from the hopper and a way to meter the amount of product that is introduced into Reaction Chamber C. In some embodiments, the valve is automated. Metering can be accomplished many ways, for example measuring the flow rate and flow time of material of known concentration leaving Hopper 1B, or measuring the weight of Hopper 1B before and after material has been transferred to Reaction Chamber C, or by transferring a quantity of material from Hopper 1B into an intermediate container that can determine the weight or volume of material introduced into it prior to further transferring the material into Reaction Chamber C.

[0124] Aspect 3—Summary of an Automated Concrete Hydration with Carbonated Water in a CO.sub.2 Rich Mixing Atmosphere.

[0125] The addition of CO.sub.2 into concrete is not new, however integrating CO.sub.2 into a combination of compounds added to the hydration water that effect the desired chemical reactions during the concrete hydration process that result in an increased percentage by weight of calcium carbonate in the completed concrete mix by hydrating the concrete with a precise blend of pH adjusted water with dissolved CO.sub.2 and mineral additives, for example calcium bicarbonate, while mixing the concrete in confined space with a precisely elevated CO.sub.2 atmosphere is new.

[0126] As previously described in detail, this process precisely meters a pre-determined amount of water and carbonate or bicarbonate salts or other additives into Reaction Chamber C as shown on FIG. 13. This is followed by precisely metering a pre-determined amount of CO.sub.2 from Reaction Chamber A or an alternative source, into Reaction Chamber C. A portion of the CO.sub.2 spontaneously reacts with the water as described in Equation 4 to make carbonic acid (H.sub.2CO.sub.3), the precursor to many carbonate reactions. The remainder of the added CO.sub.2 goes into solution within the H.sub.2O and into the headspace/atmosphere of Reaction Chamber C. This mixture of CO.sub.2 impregnated H.sub.2O with dissolved salts, for example calcium bicarbonate, is then either introduced into Reaction Chamber D or to one or more copies of Hopper 5 or other devices. When the mixture made in Reaction Chamber C is made to hydrate concrete it is introduced into Reaction Chamber D at the appropriate time in the mix cycle. When the mixture made in Reaction Chamber C is used to pre-coat aggregate, high-surface-area polymer or other concrete additives, it is pumped to one or more devices designed to coat concrete materials with CaCO.sub.3 or other minerals as described later in this document. At the completion of the CaCO.sub.3 coating process, the end product is stored in one of the Hopper 5 devices

[0127] The CO.sub.2 impregnated water with mineral enhancement contribute to the concrete in three fundamental ways: (a) the CO.sub.2 and H.sub.2CO.sub.3 in the hydration water provide a more efficient method of creating CaCO.sub.3 and other crystalized minerals within the concrete mix, and these enhance the concrete strength and chemical resistance as previously described in detail, and (b) carbonate, bicarbonate, hydroxides, CO.sub.2, and other compounds are used to adjust the pH of the hydration water and that determines which of the three processes, forming, dissolving, and precipitating CaCO.sub.3 as described in Equations 3, 4 & 5, will occur. The deliberate control of process pH directly influences the effectiveness of CaCO3 coating on aggregate, high surface polymer and other components of the concrete mix, (c) the carbonate, bicarbonate, hydroxides, CO.sub.2, and other additives can influence the setting time, slump, and add additional concrete strength.

[0128] The CO.sub.2 concentration in the water used for concrete hydration will be consumed during reactions with the concrete mix in Reaction Chamber D. However, it can be restored by adding additional CO.sub.2 gas directly into the closed headspace/atmophere of Reaction Chamber D. The CO.sub.2 gas will re-dissolve into the water, as shown in Equation 4 (duplicated below). This can be useful when the concrete mix specification requires a protracted period of low pH in the water.

CO.sub.2H.sub.2O.fwdarw.H.sub.2CO.sub.3  [4]

[0129] The second use embodiment of Reaction Chamber C is the production of the carbonate/bicarbonate rich water used for CaCO.sub.3 coating of aggregate and/or high surface polymer stored in Hopper .sub.5. As noted earlier, both applications performed in Reaction Chamber C can use the same equipment. The primary distinction between the processes is the amount of CO.sub.2 introduced into the mix and the propensity to use calcium compounds in this second embodiment. This second embodiment requires less CO.sub.2 than the first embodiment.

[0130] Aspect 4—Additional CaCO.sub.3 Coating for Aggregate or Polymer Materials

[0131] A fourth feature described in this document is the ability to provide additional thin coats of CaCO.sub.3 and other carbonates on aggregate and/or high-surface-area polymer materials or other granular materials in the concrete mix. This pre-conditioning step enhances the amount of crystalline structure provided by CaCO.sub.3 in the final concrete mix.

[0132] The compound CaCO.sub.3 is the material of choice for surface coating, but its low solubility in water (0.013 g/L (25° C.)) complicates its application. This obstacle is overcome by transporting the calcium to the surface of materials for coating in the form of Ca(HCO.sub.3).sub.2, with its higher solubility in water (166 g/L (25° C.), and then causing the Ca(HCO.sub.3).sub.2 to transform into CaCO.sub.3 through one of several methods. One method is through the change in pH of the solution containing Ca(HCO.sub.3).sub.2 by the addition of an alkaline material, for example Ca(OH).sub.2. The increased pH causes the Ca(HCO.sub.3).sub.2 to convert to CaCO.sub.3 and then precipitate out of the solution onto nearby surfaces because of its low solubility in water. This pH driven chemical process conversion is described in FIG. 5 and is stoichiometrically described in Equation 12.

Ca(HCO.sub.3).sub.2(aq)+Ca(OH).sub.2 (s) 2CaCO.sub.3(s)+2H.sub.2O  [12]

[0133] Another method to induce the precipitation of CaCO3 from a solution containing Ca(HCO.sub.3).sub.2 involves the removal of the volume of the liquid through evaporation. As the liquid volume is reduced, CO.sub.2 dissolved in the liquid is driven off into the reaction chamber or hopper when its solubility limit in water is exceeded. The CO.sub.2 liberated into the chamber or hopper can be captured using a CO.sub.2 Capture & Repurpose process developed by Richardson. The reduction in CO.sub.2 indirectly increases the pH of the solution and that pH increase promotes the precipitation of CaCO.sub.3 as described in FIG. 5.

[0134] In all embodiments of CaCO.sub.3 deposition onto high-surface-area polymer, the deposition process is enhanced when the polymer is pretreated with chlorine dioxide (ClO.sub.2) and hydrogen peroxide (H.sub.2O.sub.2). This process developed by Zoe Harmonie is described above. The treatment has been shown to mitigate polymers' natural hydrophobic characteristic and enhances the attachment of the calcium compound that is introduced through spray or other means.

[0135] In the first embodiment (FIG. 14) of this CaCO.sub.3 depositing process, water at ambient temperature, containing bicarbonate, for example Ca(HCO.sub.3).sub.2, and CO.sub.2, is sprayed on the aggregate, sand, or high-surface-area polymer while on a conveyor leading to Hopper 5, or on a surface with vibration that causes the aggregate, sand, high-surface-area polymer, or other material to reposition itself and thereby exposing other surfaces to the spray. Once the aggregate, high-surface-area polymer, or other material is stored in Hopper 5, it is sequentially treated with dry, warm air and water containing Ca(HCO.sub.3).sub.2 and/or other carbonate compounds at ambient temperature. The warm air evaporates the water on the surfaces and as the water volume decreases, CO.sub.2 is liberated from the bicarbonate ions (HCO3.sup.−1) to produce carbonate ions (CO.sub.3.sup.−2), with a resultant increase in pH of the remaining mixture volume. Stated another way, the increase in liquid pH promotes the conversion of Ca(HCO.sub.3).sub.2 into CaCO.sub.3 that precipitates on a nearby surface. This repeated pair of activities will promote the development of a carbonate film on the aggregate and/or high surface polymer. The CaCO.sub.3 that adheres to the hopper walls can be recovered and reused by dissolving it into a dilute acid, for example hydrochloric acid, and then reclaiming it from the acid by reducing the pH.

[0136] This cycle is repeated as required to build a thin layer, for example 25 microns or 50 microns of CaCO.sub.3 on the aggregate or high-surface-area polymer. It is important to terminate the process before the aggregate or high-surface-area polymer becomes fused into a solid mass that is not broken up simply by opening the gate valve on the bottom of Hopper 5.

[0137] In the second embodiment (FIG. 15) of this CaCO.sub.3 depositing process, water at ambient temperature containing bicarbonate, for example Ca(HCO.sub.3).sub.2 and/or other carbonates, is pumped into Hopper 5, or some other vessel to a depth that covers the aggregate or high-surface-area polymer. The water/carbonate mix is drained after wetting the aggregate/high-surface-area polymer. After the liquid is drained from Hopper 5, or other vessel, Hopper 5 or the other vessel is exposed to warm dry air or other gases. The aeration continues as long as required to dry the aggregate/high-surface-area polymer surfaces. The warm air evaporates water on the surfaces of the aggregate/high-surface-area polymer, or other concrete material, and as the water volume decreases, CO.sub.2 is liberated from the bicarbonate ions (HCO.sub.3.sup.−) to produce carbonate ions (CO.sub.3.sup.−2), with resultant increase in pH of the remaining mixture volume. The increase in liquid pH promotes the conversion of Ca(HCO.sub.3).sub.2 into CaCO.sub.3 which will precipitate onto nearby surfaces. This repeated pair of activities will promote the development of a carbonate film on the aggregate and/or high-surface-area polymer.

[0138] This cycle is repeated as required to build a thin layer, for example 25 microns or 50 microns of CaCO3 on the aggregate or high-surface-area polymer. It is important to terminate the process before the aggregate or high-surface-area polymer becomes fused into a solid mass that is not broken up simply by opening the gate valve on the bottom of Hopper 5. The CaCO.sub.3 that adheres to the hopper walls can be recovered and reused by dissolving it into a dilute acid, for example hydrochloric acid and then reclaiming it from the acid by reducing the pH.

[0139] Hopper 5 is specifically designed to accomplish this task by having one or more vertical channels that are narrow enough to allow gas to pass through them without high differential pressure. It also has a spring-loaded check valve at the top of and along the full length of each vertical channel. This device prevents the CO.sub.2 rich air from exiting the vessel. The bottom portion of each hopper fill chute section contains a check valve assembly. The chute is deliberately long enough to become buried in the aggregate/high-surface-area polymer when the channel is full. The protrusion of the chute into the aggregate/high-surface-area polymer prevents the recirculated air from bypassing the aggregate.

[0140] The Hopper 5 assembly includes the ability to heat air. The air is preferably heated by use of a heat exchanger coupled with a thermal source like waste heat from combustion exhaust or heat from liquid heated using an environmentally friendly technology like solar. See FIG. 13 for details on Hopper 5.

[0141] Key to FIG. 14

TABLE-US-00001 KEY DESCRIPTION A Carbonated mineral water generator (Reaction Chamber C on FIG. 13) B Heating device or heat exchanger for air, ideally using waste heat. C Warm air or air with high humidity from carbonated mineral water generator. D Chute assembly for introduction of aggregate/high-surface-area polymer. E Aggregate and/or high surface-area-polymer. F1 Closed valve used to introduce aggregate/polymer into hopper F2 Open valve used to introduce aggregate/polymer into hopper. G Closed valve used to release aggregate/polymer from hopper into Reaction Chamber D. H Blower to circulate the conditioned air through the aggregate/polymer. J Valves used to redirect air flow between two ventilation cycles.

[0142] Key to FIG. 15

TABLE-US-00002 KEY DESCRIPTION A Carbonated mineral water generator (Reaction Chamber C on FIG. 13) B Alkaline water storage and dosing system. C Air or other gas with repeating 4-step sequential treatment: (a) aerosol containing alkaline liquid; then (b) dry air(gas); then (c) aerosol containing calcium liquid; then (d) dry air (gas). D Chute assembly for introduction of aggregate/high-surface-area polymer. E Aggregate and/or high-surface-area polymer. F1 Closed valve used to introduce aggregate/polymer into hopper. F2 Open valve used to introduce aggregate/polymer into hopper. G Closed valve used to release aggregate/polymer from hopper into Reaction Chamber D. H Blower to circulate the conditioned air through the aggregate/polymer. J Air (gas) dehumidifier using desiccant (or other method) with desiccant regeneration unit.

[0143] In the third embodiment of this CaCO.sub.3 enhancement for aggregate and high-surface-area polymer, the precipitation of CaCO.sub.3 is promoted by pretreating the aggregate or other material with a caustic aqueous solution, for example calcium hydroxide (Ca(OH).sub.2). This treatment is followed exposing the aggregate or other concrete mix component with a liquid containing Ca(HCO.sub.3).sub.2. The aggregate or other compound is then exposed to dry air or equal to remove water. This sequence is repeated in alternating cycles until a film of CaCO.sub.3 between 25 microns or 50 microns is deposited on the aggregate or other concrete component. The compounds can be introduced to the aggregate or other material as a mist or as a liquid according to procedures previously described.

[0144] In the fourth embodiment of this CaCO.sub.3 enhancement for sand, small aggregate, and high-surface-area polymer occurs by lifting the target materials into the air with warm air or other gas that alternately contains an alkaline material, for example Ca(OH).sub.2 and Ca(HCO.sub.3).sub.2. Warm air without moisture is used after the Ca(HCO.sub.3).sub.2 (for example). This warm air will dry the granular material between alternating treatments. See FIG. 16 for details.

[0145] Key to FIG. 16

TABLE-US-00003 KEY DESCRIPTION A Exhaust plenum for gas fumes generated during the coating process below. B Screen & filter to prevent particles and coated objects from leaving the coating chamber. C Coating chamber. It can be any conical shape. D Suspended objects. The lifting air pressure dissipates with elevation because the area of the cone is larger. This causes the lifted objects to fall back into the chamber. E Warm dry gas used to lift coated objects up into the spray in upper areas of conical coating chamber. F Collected objects in the process of becoming coated when lifted into the upper area of the conical coating chamber. G Screen that prevents particles and objects from falling into the lower air plenum. H Plenum of hot air used to lift the particles and objects into the upper area of the conical coating chamber. I Exhaust gas duct to air filtration / scrubbing device. J Spray coating nozzle. K Warm gas entering plenum and used to lift objects and particles.

[0146] The production of concrete using this technology begins when materials are introduced into Reaction Chamber D as described on FIG. 13. This occurs in the following sequence: (a) opening a valve on one or more Hopper 5 vessels affixed to Vessel D and allow the transfer of a pre-determined amount of aggregate and/or high-surface-area polymer. If more than one “Hopper 5” vessel is provided, they can contain different add mixtures, for example, one could contain stone aggregate, and another contain high-surface-area polymer. The quantity of transferred product can be determined via weigh difference in Hopper 5 or by transferring the material into or onto a weighing device; (b) at the same time, a motorized valve on Hopper 7 allows a pre-determined amount of sand (or other material) into Reaction Chamber D. The quantity of sand (or other material) transferred product from Hopper 7 can be determined via weigh difference in Hopper 7 or by transferring the material into or onto a weighing device; (c) the materials are mixed; subsequently, as mixing continues (d) a motorized valve on Reaction Chamber C opens to transfer a pre-determined amount of carbonated mineral water into Reaction Chamber D through a pipe (Item 4 on FIG. 13). The volume of transferred liquid is measured via a flow meter or other means; and (f) the requisite amount of CO.sub.2 is added into Reaction Chamber D via piping (Item 6 on FIG. 13) with valving that connects Reaction Chamber A and Reaction Chamber D. The mixing continues until the concrete components are fully integrated; then (g) with continued mixing, a valve on Hopper 8 opens and introduces a predetermined amount of portland cement, or other plasticizing compound into Chamber D. The quantity of portland cement, for example is determined by change in weight of Hopper 8 or by measuring the weight or volume of the material as it is transferred to the chamber. Hopper 8 is sealed and pressurized to allow the cement or equal to enter Chamber D without losing CO.sub.2 into the atmosphere.

[0147] The continued addition of CO.sub.2 from Reaction Chamber A via piping identified as #6 on FIG. 13 occurs at any pre-determined times during this sequence to augment CO.sub.2 consumed in Reaction Chamber D as a result of the concrete hydration process. When the product mix requirement specifies the addition of CO.sub.2, a valve is opened that allows a pre-determined quantity of gas to enter Reaction Chamber D. This can be measured by monitoring the concentration of CO.sub.2 in Reaction chamber D or by other means.

[0148] The concrete mixing continues as specified in the product mix procedure. CO.sub.2 addition is discontinued several minutes prior to the end of the mix so the CO.sub.2 in Reaction Chamber D headspace can be integrated into the product mix before the valve on Reaction Chamber D is opened to release the finished product into “E” as specified on FIG. 13. This process prevents release of CO.sub.2 into the atmosphere. When mixing is complete, the process is complete, and the finished concrete is ready to leave Reaction chamber D and be used on a construction project.

[0149] If an automated process control system is included in the equipment package, the affiliated sensors provide process progress data that the control logic utilizes to time the mixing events, regulate the rate and amount of product flow, and determine when each activity is complete. The process PLC generates a product/batch report and saves it or prints it as required.