# US 11,305,230 B1 · Direct capture of carbon dioxide from air

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- Number: US 11,305,230 B1
- Document ID: US11305230B1
- Status: Granted
- Kind: B1
- Application number: 17/525,897
- Filed: 2021-11-13
- Granted: 2022-04-19
- Earliest claimed: 2021-11-13
- Applicants: Marvin S Keshner; Erik Garth Vaaler
- Inventors: Marvin S Keshner; Erik Garth Vaaler
- Web page: https://patentgrep.com/patent/US11305230B1

## CPC

- B01D 53/62: Carbon oxides
- B01D 53/83: with moving reactants
- B01D 53/96: Regeneration, reactivation or recycling of reactants
- C01B 32/50: Carbon dioxide
- B01D 2251/304: of sodium
- B01D 2251/404: of calcium
- B01D 2251/602: Oxides
- B01D 2251/604: Hydroxides
- B01D 2253/1124: Metal oxides
- B01D 2257/504: Carbon dioxide
- B01D 2258/06: Polluted air
- Y02C 20/40: of CO2
- Y02P 20/151: Reduction of greenhouse gas [GHG] emissions, e.g. CO2
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)
- C01B: NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; {METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C}
- Y02C: CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02P: CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS

## Abstract

A system for large scale capture of atmospheric carbon dioxide while exposed to air and weather in an outdoor environment, includes a large flat slab with a perimeter wall projecting above its surface; one or more rotary fans, providing uniform, high volume, low velocity, turbulent air flow over the entire slab surface; a transport system transferring powder—a particulate material mixed with air—to and from all locations on the slab or on an overlying mesh screen, a kiln, closed to outside air, and a compressor. The transport system includes either a vacuum/deposition system or a conveyor system with one or more conveyors. The kiln heats the particulate material, delivered by the transport system from the slab, to output released carbon dioxide, previously absorbed by the particulate material in the powder, to the compressor for compression, and either the heated particulate material, or a processed version of it.

## Claims

### Claim 1

A system for large scale capture of carbon dioxide directly from atmospheric air, comprising:
a slab having a flat top surface, either of rectangular or elliptical shape defined by a length and a width, or by a radius, and having an area greater than 400 sq. m
a perimeter wall bounding the slab and projecting above the flat top surface of the slab;
one or more rotary fans, having a combined area sufficient to provide air flow to the entire slab, each fan being configured to generate uniform, high volume, low velocity, turbulent air flow over the surface of the slab;
a transport system operable to transfer powder comprising a mixture of air and a particulate material to and from all locations on the slab or on a mesh screen located above the slab, the transport system comprising either a vacuum/deposition system comprising one or more vacuum/deposition heads, or a conveyor system comprising one or more conveyors;
a kiln, closed to outside air, configured to:
heat the particulate material, after delivery to the kiln by the vacuum/deposition or conveyor system from the slab, such that carbon dioxide previously absorbed by the particulate material in the powder is released; and
provide first and second kiln outputs, the first kiln output being the released carbon dioxide, and the second kiln output comprising either the heated particulate material, or a processed version of the heated particulate material; and
a compressor configured to receive and compress the first kiln output, providing the compressed carbon dioxide as a compressor output;
wherein the system is configured to be fully operational while exposed to atmospheric air and weather in an outdoor environment.

### Claim 2 (depends on 1)

The system in claim 1, additionally comprising:
one or more stirring beams; wherein each stirring beam has a beam length equal to the length, width or radius of the slab, is positioned above the slab along the length, width or radius of the slab, and is configured to move in a direction perpendicular to the beam over the slab;
wherein each stirring beam includes a stirring mechanism operable such that, when a layer of powder comprising a mixture of air and a particulate material capable of absorbing carbon dioxide, is present on the flat top surface of the slab:
the stirring mechanism moves some of the powder in its direction of motion, and
the stirring mechanism operates on the powder layer, comprising top, middle and bottom regions, to lift particulate material from the bottom region, to break up any caked powder, to break up any surface skin on the top region, and to mix particulate material through the top, middle and bottom regions, such that a sublayer from a top surface of the powder layer to a depth of 60 μm has a concentration of the particulate material capable of absorbing carbon dioxide of at least 10% by weight.

### Claim 3 (depends on 1)

The system in claim 1, additionally comprising:
a mesh screen located at least 3 m above the concrete slab, wherein the one or more rotary fans are placed underneath the screen to blow air up through the screen; and
one or more stirring beams located above the screen, operable such that when a layer of powder comprising a mixture of air and a particulate material is present on top of the screen, air from the fan(s) blows up through the layer.

### Claim 4 (depends on 1)

The system of claim 1,
wherein when the particulate material is of a first chemical composition, capable of absorbing carbon dioxide, it is an oxide or hydroxide of a metal; and
wherein after the particulate material has absorbed carbon dioxide, it is a carbonate of the metal.

### Claim 5 (depends on 4)

The system of claim 4, wherein the metal is one of calcium, sodium, aluminum, and iron.

### Claim 6 (depends on 1)

The system of claim 1, wherein the kiln comprises:
a first chamber configured to heat the particulate material delivered thereto in a carbon dioxide atmosphere, such that after releasing carbon dioxide, an intermediate output is formed, comprising the particulate material in an intermediate chemical composition; and
a second chamber configured to process, in a water vapor atmosphere, the intermediate output, such that the second kiln output comprises the particulate material restored to the first chemical composition; and
wherein the vacuum/deposition system mixes the second kiln output with air and transfers the mixture from the kiln to the slab.

### Claim 7 (depends on 1)

The system of claim 1, wherein the kiln comprises:
a single chamber configured to heat the particulate material delivered thereto in a carbon dioxide atmosphere, such that after releasing carbon dioxide, the second kiln output is formed, comprising the particulate material in an intermediate state;
wherein the vacuum/deposition system mixes the second kiln output with air and transfers the mixture from the kiln to the slab, where the particulate material transferred thereto subsequently absorbs water vapor from the air and is restored to the first chemical composition.

### Claim 8 (depends on 1)

The system of claim 1, wherein temperature and other process parameters of the kiln are controlled, and wherein particles may be humidified to promote agglomeration, such that the particulate material pumped or conveyed to the slab comprises highly porous particles, with an average diameter in the range of 5 μm-500 μm, each particle having an effective surface area greater than 10 times the diameter of the particle squared.

### Claim 9 (depends on 6)

The system of claim 6, wherein either the first and second chambers are held at temperatures between 900° C. and 1200° C., or the first chamber is held at a temperature between 900° C. and 1200° C. and the second chamber is held at a temperature less than 500° C.

### Claim 10 (depends on 1)

The system of claim 1, additionally comprising a means for collecting local rainwater in an area surrounding the slab and providing the collected water either to the kiln, or to powder transferred from the kiln to the slab.

### Claim 11 (depends on 1)

The system of claim 1, wherein carbon dioxide and water vapor in any exhaust produced by the burning of natural gas in the kiln are captured by particulate material brought to the kiln from the slab, the captured water vapor subsequently being used to augment steam used in the kiln.

### Claim 12

A method for large scale capture of carbon dioxide directly from atmospheric air, the method comprising: creating a receptacle of large area, the receptacle comprising a slab having a flat top surface, and a perimeter wall bounding the slab and projecting above the flat top surface of the slab; depositing, by means of pumping or conveying, a powder comprising a mixture of air and a particulate material of a first chemical composition, capable of absorbing carbon dioxide, as a layer either on the flat top surface of the slab, or on a screen positioned above the slab; providing a uniform, high volume, low velocity, turbulent air flow to expose the particulate material in the deposited layer to overlying air, such that the particulate material absorbs carbon dioxide from the air; transferring, by means of pumping or conveying, the powder from the slab to and from a kiln, closed to outside air; heating the particulate material in the kiln such that carbon dioxide previously absorbed by the particulate material in the powder is released; compressing the released carbon dioxide for transport to a storage location;
pumping or moving by one or more conveyors, from the kiln to the slab, an output that comprises either the heated particulate material mixed with air or a processed version of the heated particulate material mixed with air, the processing being carried out within the kiln; and depositing the output either on the flat top surface of the slab or on a screen positioned above the slab; wherein the method is fully operable while the receptacle and any layer of powder present on or above the top surface of the slab of the receptacle are exposed to atmospheric air and weather in an outdoor environment.

### Claim 13 (depends on 12)

The method of claim 12, additionally comprising stirring the layer of powder, such that:
some of the powder is moved along the width or length or radius of the slab; and
if the layer of powder is taken as comprising top, middle and bottom regions, particulate material is lifted from the bottom region, to break up any caked powder, to break up any surface skin on the top region, and to mix particulate material through the top, middle and bottom regions, such that a sublayer from a top surface of the powder layer to a depth of 60 μm has a concentration of the particulate material capable of absorbing carbon dioxide of at least 10% by weight.

### Claim 14 (depends on 12)

The method of claim 12, wherein when the particulate material is in the first chemical composition, capable of absorbing carbon dioxide, it is an oxide or hydroxide of a metal; and
wherein after the material has absorbed carbon dioxide, it is in a second chemical composition, as a carbonate of the metal.

### Claim 15 (depends on 14)

The method of claim 14, wherein the metal is one of calcium, sodium, aluminum, and iron.

### Claim 16 (depends on 12)

The method of claim 12, wherein the kiln comprises:
a first chamber configured to heat the transferred particulate material in a carbon dioxide atmosphere, such that after releasing carbon dioxide, an intermediate output is formed, comprising the particulate material in an intermediate chemical composition; and
a second chamber configured to process, in a water vapor atmosphere, the intermediate output, such that the processed version of the heated particulate material comprises particulate material restored to the first chemical composition;
wherein the method mixes the processed version of the heated particulate material with air and returns it from the kiln to the slab.

### Claim 17 (depends on 12)

The method of claim 12, wherein the kiln comprises:
a single chamber configured to heat the transferred particulate material in a carbon dioxide atmosphere, such that after releasing carbon dioxide, the output is formed, comprising the particulate material in an intermediate chemical composition;
wherein after the output is mixed with air and pumped from the kiln to the slab, and is deposited thereupon, the particulate material absorbs water vapor from the air and is restored to the first chemical composition.

### Claim 18 (depends on 12)

The method of claim 12, wherein temperature and other process parameters of the kiln are controlled during the processing, and wherein particles in the particulate matter output from the kiln are humidified to promote agglomeration, such that the particulate material in the output pumped or otherwise conveyed from the kiln to the slab comprises highly porous particles, with an average diameter in the range of 5-500 μm.

### Claim 19 (depends on 16)

The method of claim 16, wherein either the first and second chambers are held at temperatures between 900° C. and 1200° C., or the first chamber is held at a temperature between 900° C. and 1200° C. and the second chamber is held at a temperature less than 500° C.

### Claim 20 (depends on 12)

The method of claim 12, wherein carbon dioxide and water vapor in any exhaust produced by the burning of natural gas used in the kiln are captured by particulate matter brought to the kiln from the slab, the captured water vapor subsequently being used to augment steam used in the kiln.