WO2023129170A1 - Improved biochar reinforced rubber - Google Patents
Improved biochar reinforced rubber Download PDFInfo
- Publication number
- WO2023129170A1 WO2023129170A1 PCT/US2021/065829 US2021065829W WO2023129170A1 WO 2023129170 A1 WO2023129170 A1 WO 2023129170A1 US 2021065829 W US2021065829 W US 2021065829W WO 2023129170 A1 WO2023129170 A1 WO 2023129170A1
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- WO
- WIPO (PCT)
- Prior art keywords
- biochar
- less
- ash
- composition
- particulate
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L21/00—Compositions of unspecified rubbers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K11/00—Use of ingredients of unknown constitution, e.g. undefined reaction products
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60C—VEHICLE TYRES; TYRE INFLATION; TYRE CHANGING; CONNECTING VALVES TO INFLATABLE ELASTIC BODIES IN GENERAL; DEVICES OR ARRANGEMENTS RELATED TO TYRES
- B60C1/00—Tyres characterised by the chemical composition or the physical arrangement or mixture of the composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L9/00—Compositions of homopolymers or copolymers of conjugated diene hydrocarbons
- C08L9/06—Copolymers with styrene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K2201/00—Specific properties of additives
- C08K2201/002—Physical properties
- C08K2201/005—Additives being defined by their particle size in general
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
Definitions
- filler In the case of tires and other products formed of cured elastomeric compositions, a major component is the filler.
- these fillers include silica and carbon black, both of which are derived from nonrenewable sources. Production of carbon black results in the release of 3 kg of CO2, in addition to nitrous and sulfurous pollutants for each kg of carbon black produced. No commercially available fillers match carbon black’ s performance as a filler and improve sustainability.
- biochar from pine wood, com stover and other sources can be used to reinforce rubber compositions, provided that (a) a suitable solvent is used in grinding, for example ethanol and (b) a proton- acceptor covering agent is used to block the biochar pores, for example DPG as described in Patent Publication WO2021138444A1. What has not been determined is what sort of biochar is optimal for use in rubber.
- fillers and methods to produce them which can be produced from renewable sources and whose properties approach that of carbon black.
- Such fillers may be used in the manufacture of tires and tire components, such as bead fillers, gum strips, skim stock for the formation of belt and carcass layers reinforced with elongate textile or metal reinforcements, as well as the manufacture of other elastomeric products, such as conveyor belts, gaskets, tractor treads, for example.
- the resulting sub-micron ground biochar may be used in any elastomeric composition (either in the form of a cured composition or as a mixture for forming the cured composition) as a complete substitute for any non-renewable filler, such as carbon black and silica, for example, such that the elastomeric composition is free of any non-renewable filler, such as carbon black and silica.
- the sub-micron ground biochar may be used with reduced amounts of any such non-renewable fillers to form an elastomeric composition.
- any such elastomeric composition using the sub-micron ground biochar contemplated herein may be used for any elastomeric product utilizing elastomeric compositions that must be cured (that is, vulcanized), such as any tire tread or other tire component, gasket, conveyor belt, etc.
- the elastomeric composition such as natural or synthetic rubber, for example, using renewable sources as described and contemplated herein utilizes biochar as a filler.
- Biochar which is also referred to as pyrolyzed biomass, may be formed using any biomass, such as wood (e.g., pine wood and wood residue), com stover, wheat straw, oat hulls, rice husk, manure, switchgrass, miscanthus, lignin, and bamboo, for example.
- wood e.g., pine wood and wood residue
- com stover e.g., com stover
- wheat straw e.g., oat hulls
- rice husk oat hulls
- manure e.g., switchgrass, miscanthus, lignin, and bamboo
- biochar as a filler in elastomeric compositions has been hindered by various problems and it has been observed that the selection of the biomass affects its suitability as a rubber filler.
- as-synthesized biochar consists of particles comprised of carbon, plus additional minerals or “ash”. It has been observed that low ash concentrations in the biochar are desirable for useful properties in the biochar composites, and low ash biochar results favorable properties in the rubber composition when used as a filler compared to biochar containing higher ash content.
- Peterson, S.C. Utilization of low-ash biochar to partially replace carbon black in styrene-butadiene rubber composites. Journal of Elastomers & Plastics, 2013.
- an environmentally friendly biochar having less than 15% ash content and less than 5% elemental nitrogen content.
- a curable elastomeric composition for use in a cured elastomeric product containing an elastomer, 1 to 200 phr of a biochar filler formed of a particulate and one or more curatives, wherein the biochar filler contains less than 15% ash and less than 5% elemental nitrogen.
- biochar filler contains less than 5% ash and less than 1 % elemental nitrogen.
- biochar filler contains less than 3% ash and less than 0.5% elemental nitrogen.
- FIG. 1 provides a plot of the tensile modulus of rubber prepared with different types of biochar filler.
- biochar particles having a low ash content, combined with a low nitrogen content and used as a filler in an elastomeric compound exhibit surprisingly improved properties. Additionally, the properties are observed to be better when the biochar is comprised of particles less than 0.4 pm (micron) diameter. Additionally, it has been observed that the properties are improved while using a grinding method in ethanol.
- Biochar Preparation and Pyrolysis The biochar is prepared by selecting a biomass feedstock then desiccating by warming the biomass to remove water. Then the biomass is then pulverized to reduce the particle size. The pulverized biomass is pyrolyzed in an oxygen deprived atmosphere and allowed to cool. The resulting biochar is passed through a screen to obtain fine biochar particles.
- biochar was prepared by selecting the biomass feedstock then drying the feedstock in an oven to remove moisture from the feedstock.
- the moisture was considered “removed” when a constant mass is obtained over time after being placed in an oven at 105 °C, indicating that the moisture has been removed. It is appreciated that other methods may be used to remove the water, including, for example, placing the biochar in an oven heated to 150°C for two hours.
- the biomass was then pulverized to 2 mm or smaller sized particles in preparation for pyrolysis by use of a soil grinder to obtain the desired particle size. It should be noted that any suitable grinder may be used. Pyrolysis was accomplished under a nitrogen blanket at 700°C for one hour.
- pyrolysis was achieved by placing 50 g of desiccated biomass feedstock was placed into steel tubes and pyrolyzed under a 0.5 L/min nitrogen flow at 700 °C for one hour. The pyrolyzed biochar was allowed to cool to room temperature (approximately 22°C) before being passed through a 425 pm sieve.
- Biochar Grinding of Biochar.
- the biochar particles are then ground in a solvent and allowed to dry. This is accomplished by further grinding the particles and passed through a 100 pm size sieve.
- the particles are then ground in a solvent using spherical media in an agitated media mill and dried.
- the biochar having a particle size of 100 pm or larger was ground using a conical bur mill.
- the biochar was passed through a 100 pm sieve and 15 g of which was placed into a 500 cc stainless steel milling jar with 750 g of 1 mm diameter ceramic beads (YSZ media) and 60 g of ethanol solvent.
- the biochar was ground in a ball mill for 6 hours, reversing directions halfway through. The biochar was then separated from the milling media and allowed to dry.
- the grinding fluid is substantially a solvent.
- the solvent may be an alcohol, such as ethanol, methanol, or isopropanol, for example.
- the solvent may be toluene, acetone, or water.
- the grinding fluid may be provided as necessary to achieve a desired biochar particle size, and in certain instances, the grinding fluid is provided as a ratio of grinding fluid mass to biochar mass of 2: 1 to 15: 1.
- Particular embodiments of such methods may optionally include pregrinding the biochar composition if the biochar particulate is greater than 10% in size relative to the milling media until the biochar composition particulate is equal to or less than 10% in size relative to the milling media.
- Particular embodiments of this disclosure include a curable elastomeric composition for use in a cured elastomeric product or a cured elastomeric product itself, either such composition including an elastomer and 1 to 200 phr or more of biochar filler formed of particulate, where a majority of the particulate is less than 1 micrometer.
- One or more curatives may also be included. In other variations, 5 to 50 phr is employed.
- the curable or cured elastomeric composition is free of any non-renewable filler.
- any grinding contemplated herein may be performed using any desired process or apparatus to reduce the particle size of the biochar.
- grinding is performed by way of a milling operation using any known mill, such as a conical mill, planetary ball mill, agitated media mill, or hammermill, for example.
- grinding may be performed using a sonicator or high shear mixer in solvent but without grinding media, or in other variations with grinding media but without solvent.
- Passivating agents may be added as described in patent application publication PCT/US2020/067499.
- the particle size of biochar may be determined using any known method or apparatus.
- DCP disc centrifuge photosedimentometry
- density gradient particle sedimentation e.g., density gradient particle sedimentation
- laser light scattering e.g., dynamic or static
- light diffraction techniques may be used to determine the particle size of biochar dispersed in water, such as particle size analyzers produced by Malvern Panalytical (e.g., Mastersizer).
- Malvern Panalytical e.g., Mastersizer
- the number average may be employed to define an average particle size.
- an image analysis may be performed, such as by taking an SEM (scanning electron microscope) image at high voltage, 10 kV (kilovolts), and high magnification, such as 2,000- 10, OOOx, produce a high resolution image of the particles, with which particle sizing and counting can be performed (automatically or manually).
- the particle size measurements may be taken according to the following method, even with regard to determining post-grinding effects.
- the particle sized discussed herein may be obtained using the following method, and where such particle sizes were measured herein, the following method was employed.
- the cured elastomeric composition was cut with a Teflon coated razor blade to create a bulk sample.
- the sample was imaged using SEM at a high voltage (10 kV) to reveal the individual filler grains as opposed to the composite surface.
- the images were analyzed using the program ImageJ.
- First, two copies of the image were created: one filtered with a fine scale filter (0.05 pm radius gaussian blur) and one filtered with a coarse scale filter (1 pm radius).
- the coarse filtered image was subtracted from the fine filtered image to reveal the particles.
- the "Make Binary” function was used to create a binary image of the particles, and the "Analyze Particles" function with the "Fit Ellipse” measurement enabled was used to catalogue the particles. Particle diameters were calculated by averaging the major and minor axes of the fitted ellipses.
- Test Sample Preparation Rubber samples were cured to > 95% of the maximum modulus. The rubber was cured in 2.5 mm sheets and 75 mm dogbone samples were punched from the cured 2.5 mm rubber sheets for tensile testing. The tensile properties were measured using an Instron 5966 Extensometer at 23 °C in accordance with ASTM Standard D412 on ASTM C test pieces.
- feedstocks were examined to determine the impact of nitrogen content and ash content.
- the feedstocks are described in
- ash content biochar prepared from cow manure feedstock is highest, followed by chicken feather, com stover, canola protein, pine wood, lignin and corn starch.
- nitrogen content Canola protein is highest, followed closely by chicken feather, with corn starch being much lower.
- Table 2 The properties of organic feedstocks and biochar prepared from same.
- the tensile properties of rubber are important for performance of the finished product and are indicative of good coupling between the filler and the rubber.
- the true secant modulus of the samples is plotted in Figure 1 and summarized in Table 3.
- the ratio E300/E100 is indicative of the strength of coupling between the filler and the rubber. A value of 1 indicates poor or no coupling. A value greater than 1.5 indicates good coupling.
- the value E(break) indicates the tensile strength of the sample. A value below 5 indicates little reinforcement, while a value greater than 7 indicates sufficient reinforcement.
- true secant modulus is measured as a function of the strain or elongation, that is to say, for a given elongation, the ratio of the extension stress, divided by the true cross section of the test specimen, to the elongation.
- true secant modulus TSM F * (1 + strain)/ A/strain, where F is the force and A is the initial cross-sectional area of the test specimen.
- the true secant modulus is expressed in MPa. Breaks are shown where the true secant modulus ceases to increase and immediately drops at a particular strain.
- ash content is not the primary determinant in the properties.
- Canola protein biochar (10% ash) is only slightly different from chicken feather biochar (18% ash) and cow manure (30% ash).
- Com starch biochar (0.3% ash) is nearly identical to com stover biochar (14% ash) and cardboard (13% ash) in ash content.
- low ash content is not the determining factor for good composite tensile properties. It may be advantageous, however, for other performances.
- the biochar samples shown in Table 3 demonstrate that the chemistry has a bigger impact than the ash content of the filler, which is a surprising result. It appears that carbohydrate fillers perform well, but not as well as the lignin rich pine wood and lignin proper. The nitrogen content appears to be the most impactful chemical variable. Canola protein differs from corn starch mainly in nitrogen content. The former is non-reinforcing while the latter performs well. Similarly, chicken feather differs from com stover chiefly in nitrogen content. The com stover performs well while chicken feather does not.
- the optimal feedstock would be biochar made from low-ash, high lignin, and low nitrogen feedstock having an ash content of less than 15% and a nitrogen content of less than 5%. Alternatively, the ash content should be less than 5% and the nitrogen content less than 1%. Better yet properties are to be expected when the biochar is selected with an ash content of less than 3% and an elemental nitrogen content of less than 0.5%.
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
Claims
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US18/725,203 US20250066589A1 (en) | 2021-12-31 | 2021-12-31 | Improved biochar reinforced rubber |
| PCT/US2021/065829 WO2023129170A1 (en) | 2021-12-31 | 2021-12-31 | Improved biochar reinforced rubber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PCT/US2021/065829 WO2023129170A1 (en) | 2021-12-31 | 2021-12-31 | Improved biochar reinforced rubber |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2023129170A1 true WO2023129170A1 (en) | 2023-07-06 |
Family
ID=81327328
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/US2021/065829 Ceased WO2023129170A1 (en) | 2021-12-31 | 2021-12-31 | Improved biochar reinforced rubber |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US20250066589A1 (en) |
| WO (1) | WO2023129170A1 (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8920525B2 (en) * | 2011-04-15 | 2014-12-30 | Biogenic Reagent Ventures, Llc | High-carbon biogenic reagents and uses thereof |
| US20150196893A1 (en) * | 2014-01-16 | 2015-07-16 | Biogenic Reagent Ventures, Llc | Carbon micro-plant |
| EP2999682A1 (en) * | 2013-05-23 | 2016-03-30 | Accelergy Corporation | Producing fuels and biofertilizers from biomass |
| US20180305621A1 (en) * | 2015-03-08 | 2018-10-25 | Proton Power, Inc. | Biochar products and production |
| US20180340074A1 (en) * | 2015-11-21 | 2018-11-29 | Suncoal Industries Gmbh | Particulate carbon material producible from renewable raw materials and method for its production |
| US10927304B2 (en) | 2018-04-27 | 2021-02-23 | Thomas Jefferson University | High temperature bio-char carbonization and micron grinding and classification for inclusion into master batch polymerization |
| WO2021138444A1 (en) | 2019-12-31 | 2021-07-08 | Compagnie Generale Des Etablissements Michelin | Elastomeric composition reinforced with ground-biochar |
| WO2021234419A1 (en) * | 2020-05-22 | 2021-11-25 | Sky East Uk Ltd | Composition |
-
2021
- 2021-12-31 WO PCT/US2021/065829 patent/WO2023129170A1/en not_active Ceased
- 2021-12-31 US US18/725,203 patent/US20250066589A1/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8920525B2 (en) * | 2011-04-15 | 2014-12-30 | Biogenic Reagent Ventures, Llc | High-carbon biogenic reagents and uses thereof |
| EP2999682A1 (en) * | 2013-05-23 | 2016-03-30 | Accelergy Corporation | Producing fuels and biofertilizers from biomass |
| US20150196893A1 (en) * | 2014-01-16 | 2015-07-16 | Biogenic Reagent Ventures, Llc | Carbon micro-plant |
| US20180305621A1 (en) * | 2015-03-08 | 2018-10-25 | Proton Power, Inc. | Biochar products and production |
| US20180340074A1 (en) * | 2015-11-21 | 2018-11-29 | Suncoal Industries Gmbh | Particulate carbon material producible from renewable raw materials and method for its production |
| US10927304B2 (en) | 2018-04-27 | 2021-02-23 | Thomas Jefferson University | High temperature bio-char carbonization and micron grinding and classification for inclusion into master batch polymerization |
| WO2021138444A1 (en) | 2019-12-31 | 2021-07-08 | Compagnie Generale Des Etablissements Michelin | Elastomeric composition reinforced with ground-biochar |
| WO2021234419A1 (en) * | 2020-05-22 | 2021-11-25 | Sky East Uk Ltd | Composition |
Non-Patent Citations (6)
| Title |
|---|
| DHAR SAJIB ANINDA ET AL: "Effects of pyrolysis temperature on production and physicochemical characterization of biochar derived from coconut fiber biomass through slow pyrolysis process", BIOMASS CONVERSION AND BIOREFINERY, SPRINGER BERLIN HEIDELBERG, BERLIN/HEIDELBERG, vol. 12, no. 7, 4 November 2020 (2020-11-04), pages 2631 - 2647, XP037893052, ISSN: 2190-6815, [retrieved on 20201104], DOI: 10.1007/S13399-020-01116-Y * |
| LAY MAKARA ET AL: "Converting dead leaf biomass into activated carbon as a potential replacement for carbon black filler in rubber composites", COMPOSITES PART B, ELSEVIER, AMSTERDAM, NL, vol. 201, 23 August 2020 (2020-08-23), XP086287725, ISSN: 1359-8368, [retrieved on 20200823], DOI: 10.1016/J.COMPOSITESB.2020.108366 * |
| PETERSON, S.C.: "Utilization of low-ash biochar to partially replace carbon black in styrene-butadiene rubber composites", JOURNAL OF ELASTOMERS & PLASTICS, vol. 45, no. 5, 2013, pages 487 - 497, XP055790847, DOI: 10.1177/0095244312459181 |
| PETERSON, S.C.S. KIM: "Using Heat-Treated Starch to Modify the Surface of Biochar and Improve the Tensile Properties of Biochar-Filled Styrene-Butadiene Rubber Composites", JOURNAL OF ELASTOMERS & PLASTICS, vol. 51, no. 1, 2019, pages 26 - 35 |
| PETERSON, S.C.S.R. CHANDRASEKARANB.K. SHARMA: "Birchwood Biochar as Partial Carbon Black Replacement in Styrene-Butadiene Rubber Composites", JOURNAL OF ELASTOMERS & PLASTICS, vol. 48, no. 4, 2016, pages 305 - 316, XP002800438, DOI: 10.1177/0095244315576241 |
| XIAO, J.R. HUG. CHEN: "Micro-Nano-Engineered Nitrogenous Bone Biochar Developed With a Ball-Milling Technique for High-Efficiency Removal of Aquatic Cd (II), Cu (II) And Pb (II", JOURNAL OF HAZARDOUS MATERIALS, vol. 387, 2020, pages 121980 |
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| Publication number | Publication date |
|---|---|
| US20250066589A1 (en) | 2025-02-27 |
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