# US 10,982,162 B2 · High protein organic materials as fuel and processes for making the same

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- Number: US 10,982,162 B2
- Document ID: US10982162B2
- Status: Granted
- Kind: B2
- Application number: 16/345,151
- Filed: 2017-05-01
- Published: 2019-09-19
- Granted: 2021-04-20
- Earliest claimed: 2011-09-01
- Assignees: Akbev Group, LLC
- Applicants: Akbev Group, LLC
- Inventors: Geoffrey L. Larson; Curtis Holmes; Brandon Michael Smith; David D. Wilson
- Web page: https://patentgrep.com/patent/US10982162B2

## CPC

- C10L 5/46: on sewage, house, or town refuse {(C10L5/403, C10L5/406 take precedence)}
- C10L 5/366: {Powders}
- C10L 5/42: on animal substances or products obtained therefrom {, e.g. manure}
- C10L 5/445: {Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues}
- F23G 5/04: drying
- F23G 5/32: the waste being subjected to a whirling movement, e.g. cyclonic incinerators
- F23G 5/444: {for solid waste (F23G5/448 takes precedence)}
- F23G 7/10: of field or garden waste {or biomasses}
- C10L 2200/0259: Nitrogen containing compounds
- C10L 2200/0469: Renewables or materials of biological origin
- C10L 2200/0484: Vegetable or animal oils
- C10L 2290/02: Combustion or pyrolysis
- C10L 2290/06: Heat exchange, direct or indirect
- C10L 2290/08: Drying or removing water
- C10L 2290/148: of steam
- C10L 2290/18: Spraying or sprinkling
- C10L 2290/28: Cutting, disintegrating, shredding or grinding
- F23G 2201/20: Dewatering by mechanical means
- F23G 2201/80: Shredding
- F23G 2203/10: Stoker grate furnace
- F23G 2203/107: with vibrating grate
- F23G 2209/262: Agricultural waste
- Y02E 50/10: Biofuels, e.g. bio-diesel
- Y02E 50/30: Fuel from waste, e.g. synthetic alcohol or diesel
- C10L: FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
- F23G: CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

A process of making a fuel product from a non-combustible high protein organic material such as a biological by-product or waste material. The moisture content of the high protein organic material is mechanically reduced and dried to reduce the moisture content to less than ten percent (10%). The high protein organic material is pulverized to a particle size of less than about 2 mm. The high protein organic waste material is fed into a combustion chamber and separated during combustion such as by spraying of the high protein organic waste material within the combustion chamber. Temperature and nitrogenous hydrocarbon combustion reactions within the combustion chamber are also controlled by injection of steam within the combustion chamber.

## Claims

### Claim 1

A process for making a combustible fuel product from a non-auto-combustible organic material for a combustion system having a low nitrogen oxides (NOX) production amount and a low emissions opacity comprising the following steps:
1) providing a non-auto-combustible organic material, wherein the organic material is a high protein organic material having a protein content of about 10%, on a dry weight basis (DWB) or greater;
2) optionally mechanically removing liquid and soluble components from the high protein organic material;
3) optionally applying heat to dry the organic material to reduce its moisture content to ten percent (10%) or less by weight;
4) pulverizing the high protein organic material to reduce the high protein organic material to a particle size of less than 2 mm;
5) separating particles of the high protein organic material during a combustion phase to inhibit their cohesion into an integrated mass by spraying the particles into a combustion chamber;
6) simultaneously injecting steam into the combustion chamber to enhance combustion characteristics of the high protein organic material; and,
7) allowing protein thermal decomposition by-products to react with nitrogen oxides (NOX) within the combustion chamber to form water (H2O) and nitrogen (N2),
wherein the nitrogen oxides (NOX) production ranges from about 100 parts per million (ppm) to about 150 parts per million (ppm) and wherein the opacity of the emissions is about 20% or less on average for every 6-minute interval,
wherein the pre-combustion steps of 2) optionally mechanically removing liquid and soluble components from the high protein organic material, 3) optionally applying heat to dry the organic material to reduce its moisture content to ten percent (10%) or less by weight and, 4) pulverizing the high protein organic material to reduce the high protein organic material to a particle size of less than 2 mm may occur in any order.

### Claim 2 (depends on 1)

The process defined in claim 1, wherein pulverizing, pressing, applying heat to dry the high protein organic material particles, spraying particles into the combustion chamber and injecting steam into the combustion chamber degrades the proteins contained within the particles and denatures them by allowing nitrogen cross-linking and other cross-linking reactions to occur within the particles, allowing the particles to complete all of the cross-linking ability before the particles contact other particles.

### Claim 3 (depends on 2)

The process defined in claim 2, wherein cross-linking of the high protein organic material particles is prevented by prematurely initiating cross-linking reactions of the nitrogen bonds and other cross linking reactions while the particles are being agitated and wherein the high protein organic material particles no longer adhere to each other, thereby arresting the particles tendency to adhere to each other within the combustion chamber via nitrogen bond cross-linkage and other cross-linkage reactions.

### Claim 4 (depends on 3)

The process defined in claim 3, wherein the step of separating the high protein organic material by spraying the processed high protein organic material into the combustion chamber is effected through use of a pneumatic stoker.

### Claim 5 (depends on 4)

The process defined in claim 4, wherein spraying the particles of the high protein organic material into the combustion chamber by the pneumatic stoker keeps the particles separated in the combustion chamber long enough to allow heat transfer provided by the combustion process to quickly dry and then degrade proteins present within the high protein organic material and to prevent nitrogen cross linking and other cross linking reactions between the particles that would have the particles adhere to each other.

### Claim 6 (depends on 5)

The process defined in claim 5, wherein the particles of the high protein organic material are separated and dispersed within the combustion chamber and ignited and burned while in suspension and separated from each other before they land and adhere to each other.

### Claim 7 (depends on 6)

The process defined in claim 6, wherein the non-auto-combustible high protein organic material is rendered combustible without the addition of other combustible fuels or additives.

### Claim 8 (depends on 7)

The process defined in claim 7, wherein protein thermal decomposition by-products include ammonia, nitrogenous hydrocarbons and nitrogen-based compounds and wherein injection of ammonia, nitrogenous hydrocarbons and nitrogen-based compounds into the combustion chamber is not required to lower NOX production.

### Claim 9 (depends on 8)

The process defined in claim 8, wherein the step of mechanically removing liquid and soluble components from the high protein organic material further comprises the use of flocking agents, centrifuges, filter beds and dewatering separators.

### Claim 10 (depends on 9)

The process defined in claim 9, wherein the high protein organic material is a biological waste or by-product material.

### Claim 11 (depends on 10)

The process defined in claim 10, wherein the biological waste or by-product material originates from waste water treatment activated sludge waste and wherein the process comprises the following order of steps:
1) providing a biological waste material or by-product comprising a waste water treatment activated sludge having a protein content of about 10% or greater, on a dry weight basis (DWB);
2) removing water, moisture and other soluble components from the biological waste material or by-product;
3) drying the biological waste material or by-product to reduce the moisture content to 10% or less by weight;
4) pulverizing the biological waste material to reduce the particle size to be less than 2 mm; and
5) separating particles of the biological waste material or by-product during the combustion phase to inhibit their cohesion into an integrated mass by spraying the particles into the combustion chamber and
6) simultaneously injecting steam into the combustion chamber, wherein steam is injected to modify and control combustion reactions by reacting with nitrogen within proteins to form intermediate nitrogenous-based protein thermal combustion products which help to maintain regulatory compliance of combustion emissions.

### Claim 12 (depends on 11)

The process defined in claim 11, wherein the step of removing of water from the biological waste material or by-product comprises application of heat.

### Claim 13 (depends on 12)

The process defined in claim 12, wherein the step of drying biological waste or by-product material comprises drying the biological waste material or by-product in a heated drier, a heated progressing filter belt or other suitable drier and wherein the step of pulverizing the biological waste material or by-product comprises subjecting the biological waste material or by-product to a mill.

### Claim 14 (depends on 11)

The process defined in claim 11, wherein the high protein biological waste material or by-product is pulverized prior to drying to ensure that the high protein biological waste material has a particle size less than 2 mm.

### Claim 15 (depends on 10)

The process defined in claim 10, wherein the high protein biological waste material is hops residue and wherein the process for making the combustible fuel product from hops residue comprises the following steps in the following order:
1) extracting oils and other compounds from the ground hops utilizing mechanical separation techniques or CO2 extraction to obtain a high protein hops waste residue having a protein content of about 25 to about 30 weight percent, on a dry weight basis (DWB);
2) providing the hops waste residue;
3) drying the hops waste residue;
4) grinding the hops waste residue into a powder by pulverizing the hops waste residue to ensure that particles of the hops waste residue have a particle size of less than 2 mm;
5) agitating the hops waste residue during a combustion phase to separate particles of the hops waste residue by spraying the particles into the combustion chamber to inhibit their cohesion into an integrated mass and
6) simultaneously injecting steam into the combustion chamber to enhance the combustibility of the high protein organic material.

### Claim 16 (depends on 15)

The process defined in claim 15, wherein the step of pulverizing the hops waste residue includes subjecting the hops residue to a mill and wherein the step of drying the hops waste residue comprises the application of heat.

### Claim 17 (depends on 10)

The process defined in claim 10, wherein the high protein organic material is a high protein waste or meal from an agricultural source of oil production, waste by-products and by-products from an oil seed pulp processing.

### Claim 18 (depends on 17)

The process defined in claim 17, wherein the biological waste material comprises an oil seed pulp waste residue, further wherein the process for making a combustible fuel product from oil seed pulp waste residue comprises the following order of steps:
1) obtaining an extracted high protein oil seed pulp waste residue having a protein content of about 35%, on a dry weight basis (DWB), a moisture content of ten percent (10%) or less and a particle size less than 2 mm, wherein oil from the oil seed pulp waste residue may or may not be preliminarily extracted; and
2) separating and agitating particles of the oil seed pulp waste residue during the combustion phase to inhibit their cohesion into an integrated mass while simultaneously injecting steam into the combustion chamber.

### Claim 19 (depends on 17)

The process defined in claim 17, further comprising drying and pulverizing the oil seed pulp waste residue to ensure a moisture content of ten percent (10%) or less and a particle size of less than 2 mm.

### Claim 20 (depends on 1)

The process defined in claim 1, wherein the high protein organic material is one of a high protein animal excreta or a high protein animal meat processing by-product or waste and wherein the process comprises the following steps:
obtaining a pre-processed or “as is” high protein animal excreta or high protein animal meat processing by-product or waste which is non-auto-combustible, wherein the animal excreta has a protein content ranging from about 20% to about 60%, on a dry weight basis (DWB) and the animal meat processing by-product or waste has a protein content ranging from about 35% to about 85% dry weight basis.