EP4314198A1 - Blended fuel compositions including plastic pyrolysis oil and methods of making thereof - Google Patents
Blended fuel compositions including plastic pyrolysis oil and methods of making thereofInfo
- Publication number
- EP4314198A1 EP4314198A1 EP22714759.2A EP22714759A EP4314198A1 EP 4314198 A1 EP4314198 A1 EP 4314198A1 EP 22714759 A EP22714759 A EP 22714759A EP 4314198 A1 EP4314198 A1 EP 4314198A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- liquid product
- total liquid
- plastic pyrolysis
- vol
- fuel
- 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.)
- Pending
Links
- 238000000197 pyrolysis Methods 0.000 title claims abstract description 271
- 239000004033 plastic Substances 0.000 title claims abstract description 242
- 229920003023 plastic Polymers 0.000 title claims abstract description 242
- 239000000446 fuel Substances 0.000 title claims abstract description 171
- 239000000203 mixture Substances 0.000 title claims abstract description 100
- 238000000034 method Methods 0.000 title claims description 42
- 239000012263 liquid product Substances 0.000 claims abstract description 157
- 239000003921 oil Substances 0.000 claims abstract description 79
- 239000000295 fuel oil Substances 0.000 claims abstract description 76
- 239000003502 gasoline Substances 0.000 claims abstract description 24
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 229910052717 sulfur Inorganic materials 0.000 claims description 72
- 239000011593 sulfur Substances 0.000 claims description 72
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 70
- 238000002156 mixing Methods 0.000 claims description 45
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 claims description 22
- 229930195733 hydrocarbon Natural products 0.000 description 18
- 150000002430 hydrocarbons Chemical class 0.000 description 18
- 239000004215 Carbon black (E152) Substances 0.000 description 9
- 230000008901 benefit Effects 0.000 description 8
- 239000013502 plastic waste Substances 0.000 description 8
- 229920000642 polymer Polymers 0.000 description 8
- 239000002803 fossil fuel Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 238000009835 boiling Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- -1 and the like) Substances 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 239000010779 crude oil Substances 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 230000004907 flux Effects 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- RRHGJUQNOFWUDK-UHFFFAOYSA-N Isoprene Chemical compound CC(=C)C=C RRHGJUQNOFWUDK-UHFFFAOYSA-N 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 description 1
- 239000004677 Nylon Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000011111 cardboard Substances 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 229910052720 vanadium Inorganic materials 0.000 description 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/02—Gasoline
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/04—Diesel oil
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/06—Gasoil
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2400/00—Products obtained by processes covered by groups C10G9/00 - C10G69/14
- C10G2400/08—Jet fuel
Definitions
- the present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a traction thereof as a blending fuel and methods of making thereof.
- plastic waste For high quality recycling that leads to plastic products that can again be mechanically recycled, plastic waste must be separated by polymer type and thoroughly cleaned. Typically, plastic waste is not properly segregated and is, consequently, downgraded into inferior products that then cannot be mechanically recycled further and often will later be incinerated (Waste-to- Energy) or discarded into a landfill or the environment.
- pyrolysis An alternative to discarding plastic waste into landfills or mechanically recycling plastic waste is pyrolysis.
- Pyrolysis of plastic waste typically involves heating the plastic waste and entrained organic material in a low oxygen environment.
- a plastic pyrolysis oil having a broad boiling range can be obtained.
- Said plastic pyrolysis oil typically with additional purification processing, can be used as at least a portion of a blendstock for upgrading to plastic polymer. This pyrolysis processing provides a plastic blendstock for a more circular plastic economy.
- the present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a fraction thereof as a blending fuel.
- a first nonlimiting example method of making a blended fuel composition of the present disclosure comprises: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises about 1 vol% to about 20 vol% of the plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
- a nonlimiting example of a blended fuel composition of the present disclosure comprises: about 1 vol% to about 20 vol% of a plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
- the present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a fraction thereof as a blending fuel.
- the plastic pyrolysis oil described herein has a low oxygen content, a low sulfur content, and a high hydrocarbon content.
- blendstock fuels e.g., marine fuel, gasoline, diesel, and the like
- the plastic pyrolysis oil described herein can be used as-produced (the total liquid product) or as a distilled fraction thereof depending on the end-product fuel.
- blending hydrocarbons e.g., light cycle oil and straight run automotive diesel
- the present disclosure proposes to use plastic pyrolysis oil (total liquid product or fractions thereof) as the blending hydrocarbon.
- Blending hydrocarbons produced from crude oil and other fossil fuels can have high sulfur concentrations (depending on the source of the crude oil) but a lower cetane index, higher viscosity, and higher density as compared to the plastic pyrolysis oils described herein.
- the plastic pyrolysis oils described herein provide low-sulfur advantages (e.g., more can be added, if needed, without exceeding the final composition sulfur specifications) as well as high cetane index, lower viscosity, and lower density advantages (e.g., less plastic pyrolysis oil can be used to achieve the desired fuel properties).
- plastic pyrolysis oil All additional benefit of the use of plastic pyrolysis oil is that the rigorous requirements for mechanical recycling (e.g., separation of each plastic type and stringent pre-cleaning) are not required. Rather, several types of plastic can be pyrolyzed simultaneously with little to no precleaning because the organic matter (e.g., food) carried along with the plastic waste is also pyrolyzed.
- a reference to a “C x ” fraction, stream, portion, feed, or other quantity is defined as a fraction (or other quantity) where 50 wt% or more of the fraction corresponds to hydrocarbons having “x” number of carbons.
- a range is specified, such as “Cx-Cy,” 50 wt% or more of the fraction conesponds to hydrocarbons having a number of carbons from “x” to “y.”
- a specification of “C x +” (or “Cx-”) corresponds to a fraction where 50 wt% or more of the fraction corresponds to hydrocarbons having the specified number of carbons or more (or the specified number of carbons or less).
- plastic pyrolysis oil refers to pyrolysis oil where at least 50 wt% of the pyrolysis oil is derived from a plastic source. That is, the feedstock (also referred to as plastic feedstock) that is pyrolyzed comprises at least 50 wt% plastic.
- naphtha or “naphtha fraction’ refers to a hydrocarbon composition having an initial boiling point (ASTM D2887-19a using a using a 15-theoretical plate column and 5:1 flux ratio is a classical method to obtain the distillation curve) of about -6''C to about. 193°C.
- distillate or “distillate fraction” refers to a hydrocarbon composition having an initial boiling point ( ASTM D2887-19a using a using a 15-theoretical plate column and 5:1 flux ratio is a classical method to obtain the distillation curve) of about 193°C to about 371 °C.
- the term “heavy pyrolysis fuel” or “heavy pyrolysis fuel” refers to a hydrocarbon composition having an initial boiling point (ASTM D2887-19a using a using a 1.5- theoretical plate column and 5: 1 flux ratio is a classical method to obtain the distillation curve) of about 371 °C to about 56 PC.
- the sulfur content is measured by ASTM D2622-16.
- the metal content e.g., the amount of vanadium and other metals
- the metal content is measured by inductively couple plasma methods.
- cetane index is measured by ASTM 04737-10(2016) Procedure A,
- kinematic viscosity is measured by ASTM D445-19.
- solubility blending number (SN) and insolubility number (IN) are determined as described in US Patent No, 5,997,723, incorporated herein by reference.
- flashpoint is measured by ASTM D6450- 16a.
- CCAI calculated carbon aromaticity index
- lubricity is measured by high frequency reciprocating rig (HERR) using ASTM D6079-I8.
- NACE is a corrosion based test measured according to NACE Standard TM0 172-2001.
- Methods of the present disclosure include mixing (or blending) a plastic pyrolysis oil (e.g., a total liquid product from a plastic pyrolysis process or a fraction of the total liquid product) with a fuel oil.
- a plastic pyrolysis oil e.g., a total liquid product from a plastic pyrolysis process or a fraction of the total liquid product
- a fuel oil e.g., a fuel oil.
- plastic pyrolysis oils and blendstock fuels include, but are not limited to, a naphtha fraction of a plastic pyrolysis total liquid product and gasoline; a distillate fraction of a plastic pyrolysis total liquid product and diesel; a. distillate fraction of a plastic pyrolysis total liquid product and marine fuel; a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and marine fuel; and a plastic pyrolysis total liquid product and marine fuel.
- the amount of plastic pyrolysis oil (as the total liquid product or a fraction thereof) in a fuel may be about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1. vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol.% to about 20 vol%).
- a blended fuel composition of the present disclosure may comprise about 20 vol% or less, (or about 1 vol% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a marine fuel.
- a method of the present disclosure may comprise mixing (or blending) a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
- a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vol.% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a naphtha fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a gasoline.
- a method of the present disclosure may comprise mixing (or blending) a naphtha, fraction of plastic pyrolysis total liquid product with a gasoline in the foregoing amounts to produce a blended fuel composition.
- a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vo'1% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a distillate fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about.99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a diesel
- a method of the present disclosure may comprise mixing (or blending) a distillate fraction of a plastic pyrolysis total liquid product with a diesel in the foregoing amounts to produce a blended fuel composition.
- a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol.% to about 8 vol%. or about 10 vol% to about 20 vol%) of a distillate fraction of a plastic pyrolysis total liquid product and about. SO vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol.%) of a marine fuel.
- a method of the present disclosure may comprise mixing (or blending) a distillate fraction of a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
- a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vo1% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%.
- a method of the present disclosure may comprise mixing (or blending) a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
- the plastic pyrolysis oil may be produced on-site where the blending occurs or produced off-site and transported to the blending site.
- Pyrolysis of the plastic feedstock may be performed by known methods and in known systems (e.g, at temperatures of 400°C to 850°C, or 400°C to 600°C, or 500°C to 850°C).
- the pyrolysis process produces a gas product stream and a liquid product stream (also referred to herein as the total liquid product).
- the total liquid product is then distilled (or separated) into one or more fractions including, but not limited to, a naphtha fraction, a distillate fraction, and a heavy pyrolysis fuel fraction (e.g., comprising wax and non-distilled residue).
- plastic sources include, but are not limited to, plastic waste (e.g., plastic straws, plastic utensils, plastic bags, food containers, plastic textiles, and the like), composite materials (e.g., composite packaging), waste streams, industrial scrap, municipal waste, and the like, and any combination thereof.
- plastic waste e.g., plastic straws, plastic utensils, plastic bags, food containers, plastic textiles, and the like
- composite materials e.g., composite packaging
- waste streams industrial scrap, municipal waste, and the like, and any combination thereof.
- Said plastic sources may comprise one or more polymers that include, but are not limited to, polyolefins (e.g., homopolymer or copolymers of ethylene, propylene, butene, hexene, butadiene, isoprene, isobutylene, and other olefins), polystyrene, polyvinylchloride, polyamide (e.g., nylon), polyethylene terephthalate, polyurethane, ethylene vinyl acetate, and the like. While halogenated polymers, nitrogen-containing polymers, and oxygen-containing polymers may be used, the inclusion of said polymers is preferably minimized so that the hydrocarbon content in the plastic pyrolysis oil is maximized. Other materials may be used in combination with the plastic source to produce the plastic pyrolysis oil, for example, paper, cardboard, textiles, tissues, and the like, and any combination thereof.
- polyolefins e.g., homopolymer or copolymers of
- the plastic portion of the plastic feedstock for pyrolysis may comprise poiyolefm at 50 wt% or greater (or 65 wt% to 100 wt%, or 65 wt% to 80 wt%, or 75 wt% to 90 wt%, or 80 wt% to 100 wt%) with a balance of one or more other polymers.
- a plastic pyrolysis total liquid product may have a density of about 0.75 g/mL to about 0.90 g/mL (or about 0.75 g/mL to about 0.85 g/mL, or about 0.80 g/mL to about 0.90 g/mL).
- a plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm).
- a plastic pyrolysis total liquid product may have a kinematic viscosity at 50°C of about 1.0 mm 2 /s to about 3.0 rnniVs (or about 1.0 mm 2 /s to about 2.5 mm 2 /s, or about 2.0 mm 2 /s to about 3.0 mm 2 /s).
- a plastic pyrolysis total liquid product may have a kinematic viscosity at 100°C of about 0.5 mm 2 /s to about 2.5 mnr/s (or about 0.5 mm 2 /s to about 1.5 mm 2 /s, or about 1.0 mm 2 /s to about 2.5 mm 2 /s).
- a naph tha fracti on of a plastic pyrolysis total liquid product may have a den si ty of about
- 0.65 g/mL to about 0.80 g/mL (or about 0.65 g/mL to about 0.75 g/mL, or about 0.70 g/mL to about 0.80 g/mL).
- a naphtha fraction of a plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about. 50 ppm, or about 25 ppm to about 100 ppm).
- a distillate fraction of a plastic pyrolysis total liquid product may have a density of about 0.70 g/mL to about 0.85 g/mL (or about 0.70 g/mL to about 0.80 g/mL, or about 0.75 g/mL to about 0.85 g/mL).
- a distillate fraction of a plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm).
- a distillate fraction of a plastic pyrolysis total liquid product may have a cetane index of about 40 to about 80 (or about 40 to about 60, or abo ut 60 to about 80).
- a distillate fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 40°C of about 0.75 mm 2 /s to about 4.5 mm 2 /s (or about 0.75 mm 2 /s to about 3.5 mm 2 /s, or about 2.5 mm 2 /s to about 4.5 mm 2 /s).
- a distillate fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 100°C of about 0.25 mm 2 /s to about 2.25 .mm 2 /s (or about 0.25 mm 2 /s to about 1.5 mm 2 /s, or about 1.25 mm 2 /s to about 2.25 mm 2 /s).
- a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a density of about 0.70 g/mL to about 0.90 g/mL (or about 0.70 g/mL to about 0.85 g/mL, or about 0.75 g/mL to about 0.90 g/mL).
- a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a sulfur content of 150 ppm or less (or about 0.5 ppm to about 150 ppm, or about 0.5 ppm to about 75 ppm, or about 50 ppm to about 150 ppm).
- a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a CCAI of about 750 to about 870 (or about 750 to about 825. or about 800 to about 870).
- a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 50°C of about 3 mm 2 /s to about 20 mm 2 /s (or about 3 mm 2 /s to about 15 mm 2 /s, or about 10 mm 2 /s to about 20 mm 2 /s).
- Tables 1 and 2 below disclose properties for light cycle oils (LCO) and straight run diesels (SRD) for comparison to the plastic pyrolysis oils described herein.
- the blended fuel composition produced by mixing the plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel.
- Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less (or about 0.05 wt% to about 3 wt%); (c) a CCA I of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm 2 /s to about 700 mm 2 /s (or about 5 mm 2 /s to about 100 mm 2 /s, or about 50 mm 2 /s to about 250 mm 2 /s, or about 200 mm 2 /s to about 500 mm 2 /s, or about 400 mm 2 /s to about 700 mm 2 /s).
- the blended fuel composition produced by mixing the naphtha fraction of a plastic pyrolysis total liquid product and the gasoline may have properties desirable for a gasoline.
- Said blended gasoline properties may include one or more of the following: (a) a. density of about 0.7 g/mL to about 0.75 g/mL; and (b) a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm ).
- the blended fuel composition produced by mixing the distillate fraction of a plastic pyrolysis total liquid product and the diesel may have properties desirable for a diesel .
- Said blended diesel properties may include one or more of the following: (a) a density of about 0.8 g/mL to about 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less (or about 0.0002 wt% to about 0.002 wt%); (c) a cetane index of about 40 to about 60; and (d) a kinematic viscosity at 50°C of about 1.5 mm 2 /s to about 4.0 mm 2 /s (or about 1.5 rnm 2 /s to about 3.0 mm 2 /s, or about 2.5 rmn 2 /s to about 4.0 mm 2 /s).
- the blended fuel composition produced by mixing the distillate fraction of a plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel.
- Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1.
- the blended fuel composition produced by mixing the heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel.
- Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less (or about 0.05 wt% to about 3 wt%); (c) a CCA1 of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm 2 /s to about 700 mm 2 /s (or about 5 mm 2 /s to about 100 mm 2 /s, or about 50 mnr/s to about 250 mm 2 /s, or about 200 mm 2 /s to about 500 mm 2 /s, or about 400 mm 2 /s to about 700 mm 2 /s).
- a first nonlimiting example embodiment of the present disclosure is a method comprising: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises about 1 vol% to about 20 vol% of the plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
- a second nonlimiting example embodiment of the present disclosure is a blended fuel composition
- a blended fuel composition comprising: about 1 vol% to about 20 vol% of a plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total Liquid product and a marine iuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel
- the first and second nonlimiting example embodiment may further include one or more of: Element 1 : wherein the blended fuel composition comprises about 5 vol% to about 10 vol% of the plastic pyrolysis oil and about 90 vol% to about 95 vol% of the blendstock fuel; Element 2: wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density of about 0.75 g/mL to about 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of about L0 mm 2 /s to about 3.0 mm 2 /s; and (d) a kinematic viscosity at 100°C of about 0.5 mm 2 /s to about.
- Element 1 wherein the blended fuel composition comprises about 5 vol% to about 10 vol% of the plastic pyrolysis oil and about 90 vol% to about 95 vol%
- Element 3 Element 2 and wherein the combination is the plastic pyrolysis total liquid product and the marine fuel and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0,88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CC Al of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm 2 /s to about 700 mm 2 /s; Element 4: wherein the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the naphtha fraction has one or more of the following properties: (a) a density of about 0.65 g/mL to about 0,80 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of about 40 to about 80; (d) a
- Element I in combination with Element 2 and optionally Element 3; Element 1 in combination with Element 4 and optionally Element 5; Element 1 in combination with Element 6 and optionally Element 7; Element 1 in combination with Element 6 and optionally Element 8; and Element 1 in combination with Element 9 and optionally Element 10.
- compositions and methods are descri bed herein in terms of “comprising” various components or steps, the compositions and methods can also “consist essentially of’ or “consist of” the various components and steps.
- Tables 3-13 provide the properties an Initial fuel oil (blendstock) and a pyrolyzed plastic oil used to produce a variety of blended fuel compositions, whose properties are also provided in Tables 3-13. More specifically, Tables 3-5 are blends of marine fuel having different sulfur contents with plastic pyrolysis total liquid product; Tables 6-8 are blends of marine fuel having different sulfur contents with the heavy fraction of plastic pyrolysis total liquid product; Tables 9- 11 are blends of marine fuel having different sulfur contents with the distillate fraction of plastic pyrolysis total liquid product; Table 12 is a blend of diesel with the distillate fraction of plastic pyrolysis total liquid product; and Table .13 is a blend of gasoline with the naphtha, fraction of plastic pyrolysis total liquid product.
- Tables 3-5 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 vol% of plastic pyrolysis total liquid product. Further, high concentrations of plastic pyrolysis total liquid (e.g., 10 vol% to .15 vol%) reduces the sulfur content of the marine fuel. Further, these examples illustrate that the plastic pyrolysis total liquid product without further processing, which would typically be required of fossil fuel-derived blending hydrocarbons, can be included at concentrations of 15 vol% into marine fuels.
- Tables 6-8 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 voI% of the heavy fraction of plastic pyrolysis total liquid product. Further, high concentrations of the heavy fraction of plastic pyrolysis total liquid (e.g., 10 vol% to 15 vol%) reduces the sulfur content of the marine fuel. Additionally, these examples illustrate that the heavy fraction of a plastic pyrolysis total liquid product can be included at concentrations of 15 vol% into marine fuels.
- Tables 9-1 1 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 vol% of the distillate fraction of plastic pyrolysis total liquid product. Further, high concentrations of the distillate fraction of plastic pyrolysis total liquid (e.g., 10 vol% to 15 vol%) reduces the sulfur content of the marine fuel. Additionally, these examples illustrate that the distillate fraction of a plastic pyrolysis total liquid product can be included at concentrations of 15 vol% into marine fuels.
- Table 12 illustrates that a distillate fraction of plastic pyrolysis total liquid product can be blended with an ultra-low sulfur diesel to increase the cetane index and decrease the density while minimally increasing the sulfur content.
- fossil fuel-derived blending hydrocarbons would likely need io undergo significant and cosily desulfurization to be used with ultra-low sulfur diesel. Further, said fossil fuel-derived blending, hydrocarbons would likely have a higher density (e.g,, Table 1 and Table 2) and the reduction in density benefits of Table 3 would not be realized.
- Table 13 illustrates that a distillate fraction of plastic pyrolysis total liquid product can be blended with an ultra-low sulfur diesel to increase the cetane index and decrease the density while minimally increasing the sulfur content.
- fossil fuel-derived blending hydrocarbons would likely need io undergo significant and cosily desulfurization to be used with ultra-low sulfur diesel. Further, said fossil fuel-derived blending, hydrocarbons would likely have a higher density (e.g, Table 1 and Table 2) and the reduction in density benefits of
- Fable 13 illustrates that the naphtha traction of plastic pyrolysis total, liquid product can be blended with gasoline fuel to reduce the density.
- Tables 3-13 illustrate that plastic pyrolysis (total liquid product or a .fraction thereof) can be blended with a variety of blendstock fuels (e.g., marine fuel, naphtha fuel, and diesel) in varying concentrations, including at 15 vol%, to tune the density, viscosity, and other properties while producing a blended fuel with an acceptable low sulfur content (which in many cases is a reduced sulfur content).
- blendstock fuels e.g., marine fuel, naphtha fuel, and diesel
- compositions and methods are described in terms of “comprising,” “containing,” or “including” various components or steps, the compositions and methods can also “consist essentially of’ or “consist, of’ the various components and steps. All numbers and ranges disclosed above may vary by some amount. Whenever a numerical range with a lower limit and an upper limit is disclosed, any number and any included range falling within the range is specifically disclosed. In particular, every range of values (of the form, “from about a to about b,” or, equivalently, “from approximately a to b,” or, equivalently, “from approximately a-b”) disclosed herein is to be understood to set forth every number and range encompassed within the broader range of values.
- a method of making a blended fuel composition comprising: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises 1 vol% to 20 vol% of the plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selec ted from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and, the plastic pyrolysis total liquid product and the marine fuel.
- the plastic pyrolysis oil is the plastic pyrolysis total liquid product
- the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density' of 0.75 g/mL to 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of 1 .0 mm 2 /s to 3.0 mm 2 /s; and (d) a kinematic viscosity at 100°C of 0.5 mm 2 /s to 2.5 mm 2 /s.
- the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the naphtha fraction has one or more of the following properties: (a) a density of 0.65 g/mL to 0.80 g/mL; Cb) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 50°C of 0.5 mm 2 /s to 2.5 mm 2 /s; and (e) a kinematic viscosity at 100°C of 0. 1 mm 2 /s to 2.0 mm 2 /s. [0082] 5. The method of clause 4.
- the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.7 g/mL to 0.75 g/mL; and (b) a sulfur content of 100 ppm or less.
- the distillate fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid, product, and wherein the distillate fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 40°C of 0.75 mm 2 /s to 4.5 mm 2 /s; and (e) a kinematic viscosity at 100°C of 0.25 mm 2 /s to 2.25 mm 2 /s,
- the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1 .1 g/mL; (b) a sulfur content of 3 wt.% or less; (c) a CCAI of 750 to 870: and (d) a kinematic viscosity at 50°C of 5 mm 2 /s to 700 mm 2 /s.
- a blended fuel composition comprising: 1 vol% to 20 vol% of a plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha- fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
Abstract
Provided is a blended fuel composition including the total liquid product of a plastic pyrolysis oil or a fraction thereof and a method of making such a blended fuel composition. The blended fuel composition may include about 1 vo1% to about 20 vol% of a plastic pyrolysis oil and about 80 vol.% to about 99 vol% of the blendstock fuel. The combination of the plastic pyrolysis oil and. the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
Description
BLENDED FUEL COMPOSTIONS INCLUDING PLASTIC PYROLYSIS OIL AND
METHODS OF MAKING- THEREOF
FIELD
[0001] The present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a traction thereof as a blending fuel and methods of making thereof.
BACKGROUND
[0002 ] For high quality recycling that leads to plastic products that can again be mechanically recycled, plastic waste must be separated by polymer type and thoroughly cleaned. Typically, plastic waste is not properly segregated and is, consequently, downgraded into inferior products that then cannot be mechanically recycled further and often will later be incinerated (Waste-to- Energy) or discarded into a landfill or the environment.
[0003] An alternative to discarding plastic waste into landfills or mechanically recycling plastic waste is pyrolysis. Pyrolysis of plastic waste typically involves heating the plastic waste and entrained organic material in a low oxygen environment. Depending on the conditions of pyrolysis, a plastic pyrolysis oil having a broad boiling range can be obtained. Said plastic pyrolysis oil, typically with additional purification processing, can be used as at least a portion of a blendstock for upgrading to plastic polymer. This pyrolysis processing provides a plastic blendstock for a more circular plastic economy.
[0004] While there are many applications for plastic pyrolysis oil, applications that require minimal or no further processing after pyrolysis would the most economically beneficial while stil l providing a path to a more circular plastic economy.
SUMMARY
[0005] The present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a fraction thereof as a blending fuel.
[0006] A first nonlimiting example method of making a blended fuel composition of the present disclosure comprises: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises about 1 vol% to about 20 vol% of the plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the
plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
[0007] A nonlimiting example of a blended fuel composition of the present disclosure comprises: about 1 vol% to about 20 vol% of a plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
DETAILED DESCRIPTION
[0008] The present disclosure relates to blended fuel compositions that include plastic pyrolysis oil including the total liquid product or a fraction thereof as a blending fuel. Advantageously, the plastic pyrolysis oil described herein has a low oxygen content, a low sulfur content, and a high hydrocarbon content. Such a composition allows for the plastic pyrolysis oil (total liquid product or fractions thereof) to be blended with blendstock fuels (e.g., marine fuel, gasoline, diesel, and the like), which have low-sulfur requirements and low-oxygen preferences. Further, the plastic pyrolysis oil described herein can be used as-produced (the total liquid product) or as a distilled fraction thereof depending on the end-product fuel.
[0009] Typically, fuels are blended with other hydrocarbon liquids to produce a blended fuel composition having desired properties.. The blending hydrocarbons (e.g., light cycle oil and straight run automotive diesel) often are produced using catalytic cracking of crude oil or other fossil fuel sources. The present disclosure proposes to use plastic pyrolysis oil (total liquid product or fractions thereof) as the blending hydrocarbon. Blending hydrocarbons produced from crude oil and other fossil fuels can have high sulfur concentrations (depending on the source of the crude oil) but a lower cetane index, higher viscosity, and higher density as compared to the plastic pyrolysis oils described herein. Because of the lower cetane index, higher viscosity, and higher density, more fossil fuel-derived blending hydrocarbons (as compared to the plastic pyrolysis oils described herein) are needed to achieve the desired properties of the resultant blended fuel composition. However, the sulfur content can limit the amount of the fossil fuel-derived blending hydrocarbon that can be used. Alternatively, additional desulfurization must be performed before blending. Therefore, the plastic pyrolysis oils described herein provide low-sulfur advantages (e.g., more can be added, if needed, without exceeding the final composition sulfur specifications) as well as high cetane index, lower viscosity, and lower density advantages (e.g., less plastic pyrolysis
oil can be used to achieve the desired fuel properties). This provides enhanced versatility in the application of plastic pyrolysis oils in fuel blending. For example, naphtha, distillate, and heavy pyrolysis fuel fractions of the total liquid product of a plastic pyrolysis oil can be blended into gasoline, diesel, and marine fuel, respectively.
[0010] Other organic and biomass pyrolysis oils have been used in the production of fuel products. For example, pyrolysis of organic blendstocks like cellulose can produce broad boiling range hydrocarbon species. However, because of the blendstock composition, the resultant pyrolysis oil has a higher oxygen content, which limits the amount of said pyrolysis oil that can be included in the fuel product. In contrast, the plastic pyrolysis oil contains very low oxygen and sulfur, which allows for the plastic pyrolysis oil or a distillate thereof to be blended directly into fuel without additional purification (e.g., sulfur removal) and to be blended into the fuel at higher concentrations.
[0011] All additional benefit of the use of plastic pyrolysis oil is that the rigorous requirements for mechanical recycling (e.g., separation of each plastic type and stringent pre-cleaning) are not required. Rather, several types of plastic can be pyrolyzed simultaneously with little to no precleaning because the organic matter (e.g., food) carried along with the plastic waste is also pyrolyzed.
Definitions and Test Methods
[0012] All numerical values within the detailed description and the claims herein are modified by “about” or “approximately” the indicated value, and take into account experimental error and variations that would be expected by a person having ordinary skill in the art.
[0013] As used herein, a reference to a “Cx” fraction, stream, portion, feed, or other quantity is defined as a fraction (or other quantity) where 50 wt% or more of the fraction corresponds to hydrocarbons having “x” number of carbons. When a range is specified, such as “Cx-Cy,” 50 wt% or more of the fraction conesponds to hydrocarbons having a number of carbons from “x” to “y.” A specification of “Cx+" (or “Cx-”) corresponds to a fraction where 50 wt% or more of the fraction corresponds to hydrocarbons having the specified number of carbons or more (or the specified number of carbons or less).
[0014] As used herein, “plastic pyrolysis oil” refers to pyrolysis oil where at least 50 wt% of the pyrolysis oil is derived from a plastic source. That is, the feedstock (also referred to as plastic feedstock) that is pyrolyzed comprises at least 50 wt% plastic.
[0015] As used herein, the term “naphtha” or “naphtha fraction’’ refers to a hydrocarbon composition having an initial boiling point (ASTM D2887-19a using a using a 15-theoretical plate
column and 5:1 flux ratio is a classical method to obtain the distillation curve) of about -6''C to about. 193°C.
[0016] As used herein, the term “distillate” or “distillate fraction” refers to a hydrocarbon composition having an initial boiling point ( ASTM D2887-19a using a using a 15-theoretical plate column and 5:1 flux ratio is a classical method to obtain the distillation curve) of about 193°C to about 371 °C.
[0017] As used herein, the term “heavy pyrolysis fuel” or “heavy pyrolysis fuel” refers to a hydrocarbon composition having an initial boiling point (ASTM D2887-19a using a using a 1.5- theoretical plate column and 5: 1 flux ratio is a classical method to obtain the distillation curve) of about 371 °C to about 56 PC.
[0018] Herein, density is measured by ASTM D4052-18a measured at 15°C,
[0019] Herein, the sulfur content is measured by ASTM D2622-16.
[0020] Herein, the metal content (e.g., the amount of vanadium and other metals) is measured by inductively couple plasma methods.
[0021] Herein, cetane index is measured by ASTM 04737-10(2016) Procedure A,
[0022] Herein, kinematic viscosity is measured by ASTM D445-19.
[0023] Herein, solubility blending number (SN) and insolubility number (IN) are determined as described in US Patent No, 5,997,723, incorporated herein by reference.
[0024] Herein, flashpoint is measured by ASTM D6450- 16a.
[0025] Herein, calculated carbon aromaticity index (CCAI) is determined according to
Equation FJ in ISO 8217:2012.
[0026] Herein, lubricity is measured by high frequency reciprocating rig (HERR) using ASTM D6079-I8.
[0027] Herein, NACE is a corrosion based test measured according to NACE Standard TM0 172-2001.
Compositions and Methods
[0028] Methods of the present disclosure include mixing (or blending) a plastic pyrolysis oil (e.g., a total liquid product from a plastic pyrolysis process or a fraction of the total liquid product) with a fuel oil. Example combinations of plastic pyrolysis oils and blendstock fuels include, but are not limited to, a naphtha fraction of a plastic pyrolysis total liquid product and gasoline; a distillate fraction of a plastic pyrolysis total liquid product and diesel; a. distillate fraction of a plastic pyrolysis total liquid product and marine fuel; a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and marine fuel; and a plastic pyrolysis total liquid product and marine fuel.
[0029] The amount of plastic pyrolysis oil (as the total liquid product or a fraction thereof) in a fuel may be about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1. vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol.% to about 20 vol%).
(0030] For example, a blended fuel composition of the present disclosure may comprise about 20 vol% or less, (or about 1 vol% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a marine fuel. Further, a method of the present disclosure may comprise mixing (or blending) a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
[0031] In another example, a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vol.% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a naphtha fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a gasoline. Further, a method of the present disclosure may comprise mixing (or blending) a naphtha, fraction of plastic pyrolysis total liquid product with a gasoline in the foregoing amounts to produce a blended fuel composition.
[0032] In yet another example, a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vo'1% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a distillate fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about.99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a diesel Further, a method of the present disclosure may comprise mixing (or blending) a distillate fraction of a plastic pyrolysis total liquid product with a diesel in the foregoing amounts to produce a blended fuel composition. [0033] In another example, a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vol% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol.% to about 8 vol%.
or about 10 vol% to about 20 vol%) of a distillate fraction of a plastic pyrolysis total liquid product and about. SO vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%, or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol.%) of a marine fuel. Further, a method of the present disclosure may comprise mixing (or blending) a distillate fraction of a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
[9034] In yet another example, a blended fuel composition of the present disclosure may comprise about 20 vol% or less (or about 1 vo1% to about 20 vol%, or about 1 vol% to about 15 vol%, or about 1 vol% to about 10 vol%, or about 1 vol% to about 5 vol%, or about 3 vol% to about 8 vol%, or about 10 vol% to about 20 vol%) of a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and about 80 vol% or more (or about 80 vol% to about 99 vol%, or about 85 vol% to about 99 vol%, or about 90 vol% to about 99 vol%, or about 95 vol% to about 99 vol%. or about 92 vol% to about 97 vol%, or about 80 vol% to about 90 vol%) of a marine fuel Further, a method of the present disclosure may comprise mixing (or blending) a heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product with a marine fuel in the foregoing amounts to produce a blended fuel composition.
[9035] The plastic pyrolysis oil may be produced on-site where the blending occurs or produced off-site and transported to the blending site.
[0036] Pyrolysis of the plastic feedstock may be performed by known methods and in known systems (e.g, at temperatures of 400°C to 850°C, or 400°C to 600°C, or 500°C to 850°C). The pyrolysis process produces a gas product stream and a liquid product stream (also referred to herein as the total liquid product). Optionally, the total liquid product is then distilled (or separated) into one or more fractions including, but not limited to, a naphtha fraction, a distillate fraction, and a heavy pyrolysis fuel fraction (e.g., comprising wax and non-distilled residue).
[9037] Examples of plastic sources include, but are not limited to, plastic waste (e.g., plastic straws, plastic utensils, plastic bags, food containers, plastic textiles, and the like), composite materials (e.g., composite packaging), waste streams, industrial scrap, municipal waste, and the like, and any combination thereof.
[9038] Said plastic sources may comprise one or more polymers that include, but are not limited to, polyolefins (e.g., homopolymer or copolymers of ethylene, propylene, butene, hexene, butadiene, isoprene, isobutylene, and other olefins), polystyrene, polyvinylchloride, polyamide (e.g., nylon), polyethylene terephthalate, polyurethane, ethylene vinyl acetate, and the like. While halogenated polymers, nitrogen-containing polymers, and oxygen-containing polymers may be
used, the inclusion of said polymers is preferably minimized so that the hydrocarbon content in the plastic pyrolysis oil is maximized. Other materials may be used in combination with the plastic source to produce the plastic pyrolysis oil, for example, paper, cardboard, textiles, tissues, and the like, and any combination thereof.
[0039] Preferably, the plastic portion of the plastic feedstock for pyrolysis may comprise poiyolefm at 50 wt% or greater (or 65 wt% to 100 wt%, or 65 wt% to 80 wt%, or 75 wt% to 90 wt%, or 80 wt% to 100 wt%) with a balance of one or more other polymers.
[9040] A plastic pyrolysis total liquid product may have a density of about 0.75 g/mL to about 0.90 g/mL (or about 0.75 g/mL to about 0.85 g/mL, or about 0.80 g/mL to about 0.90 g/mL).
[0041] A plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm).
[0042] A plastic pyrolysis total liquid product may have a kinematic viscosity at 50°C of about 1.0 mm2/s to about 3.0 rnniVs (or about 1.0 mm2/s to about 2.5 mm2/s, or about 2.0 mm2/s to about 3.0 mm2/s).
[0043] A plastic pyrolysis total liquid product may have a kinematic viscosity at 100°C of about 0.5 mm2/s to about 2.5 mnr/s (or about 0.5 mm2/s to about 1.5 mm2/s, or about 1.0 mm2/s to about 2.5 mm2/s).
[0044] A naph tha fracti on of a plastic pyrolysis total liquid product may have a den si ty of about
0.65 g/mL to about 0.80 g/mL (or about 0.65 g/mL to about 0.75 g/mL, or about 0.70 g/mL to about 0.80 g/mL).
[0045] A naphtha fraction of a plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about. 50 ppm, or about 25 ppm to about 100 ppm).
[0046] A distillate fraction of a plastic pyrolysis total liquid product may have a density of about 0.70 g/mL to about 0.85 g/mL (or about 0.70 g/mL to about 0.80 g/mL, or about 0.75 g/mL to about 0.85 g/mL).
[0047] A distillate fraction of a plastic pyrolysis total liquid product may have a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm).
[0048] A distillate fraction of a plastic pyrolysis total liquid product may have a cetane index of about 40 to about 80 (or about 40 to about 60, or abo ut 60 to about 80).
[0049] A distillate fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 40°C of about 0.75 mm2/s to about 4.5 mm2/s (or about 0.75 mm2/s to about 3.5 mm2/s, or about 2.5 mm2/s to about 4.5 mm2/s).
[0050] A distillate fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 100°C of about 0.25 mm2/s to about 2.25 .mm2/s (or about 0.25 mm2/s to about 1.5 mm2/s, or about 1.25 mm2/s to about 2.25 mm2/s).
[0051] A heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a density of about 0.70 g/mL to about 0.90 g/mL (or about 0.70 g/mL to about 0.85 g/mL, or about 0.75 g/mL to about 0.90 g/mL).
[0052 ] A heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a sulfur content of 150 ppm or less (or about 0.5 ppm to about 150 ppm, or about 0.5 ppm to about 75 ppm, or about 50 ppm to about 150 ppm).
[0053] A heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a CCAI of about 750 to about 870 (or about 750 to about 825. or about 800 to about 870).
[0054] A heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product may have a kinematic viscosity at 50°C of about 3 mm2/s to about 20 mm2/s (or about 3 mm2/s to about 15 mm2/s, or about 10 mm2/s to about 20 mm2/s).
[0055] Tables 1 and 2 below disclose properties for light cycle oils (LCO) and straight run diesels (SRD) for comparison to the plastic pyrolysis oils described herein.
Table 1
Table 2
[0056] The blended fuel composition produced by mixing the plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel. Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less (or about 0.05 wt% to about 3 wt%); (c) a CCA I of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm2/s to about 700 mm2/s (or about 5 mm2/s to about 100 mm2/s, or about 50 mm2/s to about 250 mm2/s, or about 200 mm2/s to about 500 mm2/s, or about 400 mm2/s to about 700 mm2/s).
[0057] The blended fuel composition produced by mixing the naphtha fraction of a plastic pyrolysis total liquid product and the gasoline may have properties desirable for a gasoline. Said blended gasoline properties may include one or more of the following: (a) a. density of about 0.7 g/mL to about 0.75 g/mL; and (b) a sulfur content of 100 ppm or less (or about 0.5 ppm to about 100 ppm, or about 0.5 ppm to about 50 ppm, or about 25 ppm to about 100 ppm ).
[0058] The blended fuel composition produced by mixing the distillate fraction of a plastic pyrolysis total liquid product and the diesel may have properties desirable for a diesel . Said blended diesel properties may include one or more of the following: (a) a density of about 0.8 g/mL to about 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less (or about 0.0002 wt% to about 0.002 wt%); (c) a cetane index of about 40 to about 60; and (d) a kinematic viscosity at 50°C of about 1.5 mm2/s to about 4.0 mm2/s (or about 1.5 rnm2/s to about 3.0 mm2/s, or about 2.5 rmn2/s to about 4.0 mm2/s). |0059[ The blended fuel composition produced by mixing the distillate fraction of a plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel. Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1. g/mL; (b) a sulfur content of 3 wt% or less (or about 0.05 wt% to about 3 wt%); (c) a CCA1 of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about
5 mm2/s to about 700 mnr/s (or about 5 mm2/s to about 100 mm2/s, or about 50 mm2/s to about 250 mm2/s, or about 200 mm2/s to about 500 mn^/s, or about 400 mm2/s to about 700 mm2/s).
[0060] The blended fuel composition produced by mixing the heavy pyrolysis fuel fraction of a plastic pyrolysis total liquid product and the marine fuel may have properties desirable for a marine fuel. Said blended marine fuel properties may include one or more of the following: (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less (or about 0.05 wt% to about 3 wt%); (c) a CCA1 of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm2/s to about 700 mm2/s (or about 5 mm2/s to about 100 mm2/s, or about 50 mnr/s to about 250 mm2/s, or about 200 mm2/s to about 500 mm2/s, or about 400 mm2/s to about 700 mm2/s). Ex amp le Embodiments
[0061] A first nonlimiting example embodiment of the present disclosure is a method comprising: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises about 1 vol% to about 20 vol% of the plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
[0062] A second nonlimiting example embodiment of the present disclosure is a blended fuel composition comprising: about 1 vol% to about 20 vol% of a plastic pyrolysis oil and about 80 vol% to about 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total Liquid product and a marine iuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel
[0063] The first and second nonlimiting example embodiment may further include one or more of: Element 1 : wherein the blended fuel composition comprises about 5 vol% to about 10 vol% of the plastic pyrolysis oil and about 90 vol% to about 95 vol% of the blendstock fuel; Element 2: wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density of about 0.75 g/mL to about 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at
50°C of about L0 mm2/s to about 3.0 mm2/s; and (d) a kinematic viscosity at 100°C of about 0.5 mm2/s to about. 2.5 mm2/s; Element 3: Element 2 and wherein the combination is the plastic pyrolysis total liquid product and the marine fuel and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0,88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CC Al of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm2/s to about 700 mm2/s; Element 4: wherein the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the naphtha fraction has one or more of the following properties: (a) a density of about 0.65 g/mL to about 0,80 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of about 40 to about 80; (d) a kinematic viscosity at 50°C of about 0,5 mm2/s to about 2.5 mm2/s; and (e) a kinematic viscosity at 100*C of about 0.1 mm2/s to about 2.0 mm2/s; Element 5: Element 4 and wherein the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0.7 g/mL to about 0.75 g/mL; and (b) a sulfur content of 100 ppm or less; Element 6: wherein the distillate fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the disti llate fraction has one or more of the following properties: (a) a density of about 0.70 g/mL to about 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of about 40 to about 80; (d) a kinematic viscosity at 40°C of about 0.75 mm2/s to about 4.5 mm2/s; and (e) a kinematic viscosity at 100°C of about 0.25 mm2/s to about 2.25 mm2/s; Element 7: Element 6 and wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the diesel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0.8 g/mL to about 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less; (c) a cetane index of about 40 to about 60; and (d) a kinematic viscosity at 50°C of about 1.5 mm2/s to about 4.0 mm2/s; Element 8: Element 6 and wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties; (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CC Al of about 750 to about 870; and (d) a kinematic viscosity at 5(°C of about 5 mm2/s to about 700 mm2/s; Element 9: wherein the heavy pyrolysis fuel fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the heavy pyrolysis fuel fraction has one or more of the following properties: (a) a density of about 0.70 g/mL to about 0.90 g/mL; (b) a sulfur content of 150 ppm or less; (c) a CCAI of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 3 mm2/s to about 20 mm2/s; and Element 10; Element 9 and wherein the combination is the heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of
the following properties: (a) a density of about 0.88 g/mL to about 1 .1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm2/s to about 700 mm2/s. Examples of combinations include, but are not limited to. Element I in combination with Element 2 and optionally Element 3; Element 1 in combination with Element 4 and optionally Element 5; Element 1 in combination with Element 6 and optionally Element 7; Element 1 in combination with Element 6 and optionally Element 8; and Element 1 in combination with Element 9 and optionally Element 10.
[0064] Unless otherwise indicated, all numbers expressing quantities of ingredients, properties such as molecular weight, reaction conditions, and so forth used in the present specification and associated claims are to be understood as being modified in all instances by the term “about.” Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following specification and attached claims are approximations that may vary depending upon the desired properties sought to be obtained by the embodiments of the present disclosure. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claim, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques,
[0065] One or more illustrative embodiments incorporating the disclosure embodiments disclosed herein are presented herein. Not all features of a physical implementation are described or shown in this application for the sake of clarity. It is understood that in the development of a physical embodiment incorporating the embodiments of the present disclosure, numerous implementation-specific decisions must be made to achieve the developer’s goals, such as compliance with system-related, business-related, government-related and other constraints, which vary by implementation and from time to time. While a developer’s efforts might be time- consuming, such efforts would be, nevertheless, a routine undertaking for those of ordinary skill in the art and having benefit of this disclosure.
[0066] While compositions and methods are descri bed herein in terms of “comprising” various components or steps, the compositions and methods can also “consist essentially of’ or “consist of” the various components and steps.
[0067] It is to be understood that while the disclosure has been described in conjunction with the specific embodiments thereof, the foregoing description is intended to illustrate and not limit the scope of the disclosure. Other aspects, advantages and modifications will be apparent to those skilled in the art to which the disclosure pertains.
[0068] To facilitate a better understanding of the embodiments of the present disclosure, the following, examples of preferred or representative embodiments are given. In no way should the following examples be read to limit, or to define, the scope of the disclosure,
EXAMPLES
[0069] Tables 3-13 provide the properties an Initial fuel oil (blendstock) and a pyrolyzed plastic oil used to produce a variety of blended fuel compositions, whose properties are also provided in Tables 3-13. More specifically, Tables 3-5 are blends of marine fuel having different sulfur contents with plastic pyrolysis total liquid product; Tables 6-8 are blends of marine fuel having different sulfur contents with the heavy fraction of plastic pyrolysis total liquid product; Tables 9- 11 are blends of marine fuel having different sulfur contents with the distillate fraction of plastic pyrolysis total liquid product; Table 12 is a blend of diesel with the distillate fraction of plastic pyrolysis total liquid product; and Table .13 is a blend of gasoline with the naphtha, fraction of plastic pyrolysis total liquid product.
Table 3
* Prophetic values based on trends seen in blending fuels.
Table 4
* Prophetic values based on trends seen in blending fuels.
Table 5
* on trends seen in blending fuels.
[0070] Tables 3-5 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 vol% of plastic pyrolysis total liquid product. Further, high concentrations of plastic pyrolysis total liquid (e.g., 10 vol% to .15 vol%) reduces the sulfur content of the marine fuel. Further, these examples illustrate that the plastic pyrolysis total liquid product without further processing, which would typically be required of fossil fuel-derived blending hydrocarbons, can be included at concentrations of 15 vol% into marine fuels.
Table 6
* Prophetic values based on trends seen in blending fuels.
Table 7
£ Prophetic values based on ing fuels.
Table 8
* Prophetic values based on trends seen in blending fuels,
[0071] Tables 6-8 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 voI% of the heavy fraction of plastic pyrolysis total liquid product. Further, high concentrations of the heavy fraction of plastic pyrolysis total liquid (e.g., 10 vol% to 15 vol%) reduces the sulfur content of the marine fuel. Additionally, these examples illustrate that the heavy fraction of a plastic pyrolysis total liquid product can be included at concentrations of 15 vol% into marine fuels.
Table 9
* Prophetic values based on trends seen in blending fuels.
Table 10
S:;i\
IN
SBN-IN
* Prophetic values based on trends seen in blending fuels.
Table 11
* Prophetic values based on trends seen in blending fuels
[0072] Tables 9-1 1 illustrate that viscosity of the marine fuel blendstock can be greatly reduced with as little as 1 vol% of the distillate fraction of plastic pyrolysis total liquid product. Further, high concentrations of the distillate fraction of plastic pyrolysis total liquid (e.g., 10 vol% to 15 vol%) reduces the sulfur content of the marine fuel. Additionally, these examples illustrate that the distillate fraction of a plastic pyrolysis total liquid product can be included at concentrations of 15 vol% into marine fuels.
Table 12
- Not measured
[0073] Table 12 illustrates that a distillate fraction of plastic pyrolysis total liquid product can be blended with an ultra-low sulfur diesel to increase the cetane index and decrease the density while minimally increasing the sulfur content. In contrast, fossil fuel-derived blending hydrocarbons would likely need io undergo significant and cosily desulfurization to be used with ultra-low sulfur diesel. Further, said fossil fuel-derived blending, hydrocarbons would likely have a higher density (e.g,, Table 1 and Table 2) and the reduction in density benefits of Table 3 would not be realized.
Table 13
[0074] Fable 13 illustrates that the naphtha traction of plastic pyrolysis total, liquid product can be blended with gasoline fuel to reduce the density.
[0075] Tables 3-13 illustrate that plastic pyrolysis (total liquid product or a .fraction thereof) can be blended with a variety of blendstock fuels (e.g., marine fuel, naphtha fuel, and diesel) in varying concentrations, including at 15 vol%, to tune the density, viscosity, and other properties while producing a blended fuel with an acceptable low sulfur content (which in many cases is a reduced sulfur content).
[0076] Therefore, the present disclosure is well adapted to attain the ends and advantages mentioned as well as those that are inherent therein. The particular embodiments disclosed above are illustrative only, as the present disclosure may be modified and practiced In different but equivalent manners apparent to those skilled in the art having the benefit of the teachings herein. Furthermore, no limitations are intended to the details of construction or design herein shown, other than as described in the claims below. It is therefore evident that the particular illustrative embodiments disclosed above may be altered, combined, or modified and all such variations are considered within the scope and spirit of the present disclosure. The disclosure illustratively disclosed herein suitably may be practiced in the absence of any element that is not. specifically disclosed herein and/or any optional element disclosed herein. While compositions and methods are described in terms of “comprising,” “containing,” or “including” various components or steps, the compositions and methods can also “consist essentially of’ or “consist, of’ the various
components and steps. All numbers and ranges disclosed above may vary by some amount. Whenever a numerical range with a lower limit and an upper limit is disclosed, any number and any included range falling within the range is specifically disclosed. In particular, every range of values (of the form, “from about a to about b,” or, equivalently, “from approximately a to b,” or, equivalently, “from approximately a-b”) disclosed herein is to be understood to set forth every number and range encompassed within the broader range of values. Also, the terms in the claims have their plain, ordinary meaning unless otherwise explicitly and clearly defined by the patentee. Moreover, the indefinite articles “a” or “an,” as used in the claims, are defined herein to mean one or more than one of the elements that it introduces .
[0077] PC17EP Clauses:
[0078] 1. A method of making a blended fuel composition comprising: blending a plastic pyrolysis oil with a blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises 1 vol% to 20 vol% of the plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selec ted from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and, the plastic pyrolysis total liquid product and the marine fuel.
[0079] 2. The method of clause 1, wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density' of 0.75 g/mL to 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of 1 .0 mm2/s to 3.0 mm2/s; and (d) a kinematic viscosity at 100°C of 0.5 mm2/s to 2.5 mm2/s.
[0080] 3. The method of clause 2, wherein the combination. is the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to .1.1 g/mL; (b) a sulfur content of 3 wt.% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
[0081] 4. The method of clause I, wherein the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the naphtha fraction has one or more of the following properties: (a) a density of 0.65 g/mL to 0.80 g/mL; Cb) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 50°C of 0.5 mm2/s to 2.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0. 1 mm2/s to 2.0 mm2/s.
[0082] 5. The method of clause 4. wherein the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.7 g/mL to 0.75 g/mL; and (b) a sulfur content of 100 ppm or less.
[0083] 6. The method of clause I , wherein the distillate fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid, product, and wherein the distillate fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 40°C of 0.75 mm2/s to 4.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0.25 mm2/s to 2.25 mm2/s,
[0084] 7, Idle method of clause 6, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the diesel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.8 g/mL to 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less; (c) a cetane index of 40 to 60; and
(d) a kinematic viscosity at 50°C of 1.5 mm2/s to 4.0 mm2/s.
[0085] 8. 1 he method of clause 6, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1 .1 g/mL; (b) a sulfur content of 3 wt.% or less; (c) a CCAI of 750 to 870: and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
[0086] 9. The method of clause L wherein the heavy pyrolysis fuel fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the heavy pyrolysis fuel fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.90 g/mL; (b) a sulfur content of 150 ppm or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 3 mm2/s to 20 mm2/s.
[0087] 10. The method of clause 9, wherein the combination is the heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1 . 1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
[0088] I L A blended fuel composition comprising: 1 vol% to 20 vol% of a plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha- fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and
a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
[0089] 12. The blended fuel composition of clause 11 , wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties:. (a) a density of 0.75 g/mL to 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of 1.0 mnr/s to 3.0 mm2/s; and (d) a kinematic viscosity at 100°C of 0.5 mm2/s to 2.5 mm2/s.
[0090] 13, The blended fuel composition of clause 12, wherein the combination is the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mnr/s to 700 mm2/s.
[0091] 14. The blended fuel composition of clause 11, wherein the naphtha fraction of the plastic pyrolysis oii is the plastic pyrolysis total liquid product; and wherein naphtha fraction has one or more of the following, properties: (a) a density of 0.65 g/mL to 0.80 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 50°C of 0.5 mm2/s to 2.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0. 1 mm2/s to 2.0 mm2/s.
[0092] 15. The blended fuel composition of clause 16, wherein the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.7 g/mL to 0.75 g/mL; and (b) a sulfur content of 100 ppm or less.
[0093] 16. The blended fuel composition of clause I I, wherein the distillate fraction of the plastic pyrolysis oil Is the plastic pyrolysis total liquid product, and wherein the distillate fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 40°C of 0.75 mm2/s to 4.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0.25 mm2/s to 2.25 mm2/s. [0094] 17. The blended fuel composition of clause 16, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the diesel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.8 g/mL to 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less; (c) a cetane index of 40 to 60; and (d) a kinematic viscosity at 50°C of 1.5 mm2/s to 4.0 mm2/s.
[0095] 18. The blended fuel composition of clause 16, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0.88 g/mL to
about 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of about 750 to about 870; and (d) a kinematic viscosity at 50°C of about 5 mm2/s to about 700 mm2/s.
[0096] 19. The blended fuel composition of clause 11, wherein the heavy pyrolysis fuel fraction of the plastic pyrolysis oil Is the plastic pyrolysis total liquid product, and the heavy pyrolysis fuel fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.90 g/mL; (b) a sulfur content of 150 ppm or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 3 mm2/s to 20 mm2/s.
[0097] 20. The blended fuel composition of clause 19, wherein the combination is the heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1. 1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700
Claims
What is claimed is:
L A method of making a blended fuel composition comprising: blending a plastic pyrolysis oil with a. blendstock fuel to produce a blended fuel composition, wherein the blended fuel composition comprises 1 vol% to 20 vol.% of the plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel; the distillate fraction of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and, the plastic pyrolysis total liquid product and the marine fuel,
2. The method of claim 1, wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density of 0.75 g/mL. to 0.90 g/mL; (b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of 1.0 mm2/s to 3.0 mm2/s; and (d) a kinematic viscosity at 100°C of 0.5 mm2/s to 2.5 mm2/s.
3. The method of claim 2, wherein the combination is the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1 .1 g/mL; (b) a sul&r content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
4. The method of claim .1 , wherein the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the naphtha fraction has one or more of the following properties: (a) a density of 0.65 g/mL to 0.80 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 50°C of 0.5 mm2/s to 2.5 mm2/s; and (e) a kinematic viscosity at 1.00°C of 0,1 mm2/s to 2.0 mm2/s.
5. The method of claim 4, wherein the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.7 g/mL to 0.75 g/mL; and (b) a sul&r content of 100 ppm or less.
6. The method of claim 1, wherein the distillate fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the distillate fraction has one or more of the following properties: (a) a density of 0.70 g/ml, to 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 40°C of 0.75 mm2/s to 4.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0.25 mm3/s to 2.25 mm2/s.
7. The method of claim 6, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the diesel, and wherein the blended, fuel composition has one or more of the following properties: (a) a density of 0.8 g/niL to 0.87 gZmL; (b) a sulfur content of 0.002 wt% or less; (c) a cetane index of 40 to 60; and
(d) a kinematic viscosity at 50°C of 1.5 mm2/s to 4.0 mm2/s.
8. The method of claim 6, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel . and wherein the blended fuel composition has one or more of the following properties: (a.) a density of 0.88 g/mL to 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
9. The method of claim L wherein the heavy pyrolysis fuel fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the heavy pyrolysis fuel fraction has one or more of the following properties: (a) a density of 0.70 gZmL to 0.90 gZmL; (b) a sulfur content of 150 ppm or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 3 mm2/s to 20 mm2/s.
10. The method of claim 9, wherein the combination is the heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1 . 1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
1 L A blended fuel composition comprising: 1 vol% to 20 vol% of a plastic pyrolysis oil and 80 vol% to 99 vol% of the blendstock fuel, and wherein a combination of the plastic pyrolysis oil and the blendstock fuel is selected .from the group consisting of: a naphtha fraction of the plastic pyrolysis total liquid product and gasoline; a distillate fraction of the plastic pyrolysis total liquid product and diesel ; the distillate fraction, of the plastic pyrolysis total liquid product and a marine fuel; a heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel; and the plastic pyrolysis total liquid product and the marine fuel.
12. The blended fuel composition of claim 1 1, wherein the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein the plastic pyrolysis total liquid product has one or more of the following properties: (a) a density of 0.75 g/mL to 0.90 gZmL; ( b) a sulfur content of 100 ppm or less; (c) a kinematic viscosity at 50°C of 1.0 mnfrZs to 3.0 mm2/s; and (d) a kinematic viscosity at 100°C of 0.5 mm2Zs to 2.5 mm2Zs.
13. The blended fuel composition of claim 12, wherein the combination is the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has
one or more of the following properties: (a) a density of 0.88 g/mL to 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
14. The blended fuel composition of claim 11 , wherein the naphtha fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and wherein naphtha fraction has one or more of the following, properties: (a) a density of 0.65 g/mL to 0.80 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 50°C of 0.5 mm3/s to 2.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0.1 mm2/s to 2.0 mm2/s.
15. The blended fuel composition of claim 11 , wherein the combination is the naphtha fraction of the plastic pyrolysis total liquid product and the gasoline, and wherein the blended fuel composition has one or more of the following properties; (a) a density of 0.7 g/mL to 0.75 g/mL; and (b) a sulfur content of 100 ppm or less.
16. The blended fuel composition of claim 11, wherein the distillate fraction of the plastic pyrolysis oil Is the plastic pyrolysis total liquid product, and wherein the distillate fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.85 g/mL; (b) a sulfur content of 100 ppm or less; (c) a cetane index of 40 to 80; (d) a kinematic viscosity at 40°C of 0.75 mm2/s to 4.5 mm2/s; and (e) a kinematic viscosity at 100°C of 0.25 mm2/s to 2.25 mm2/s.
17. The blended fuel composition of claim 16, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the diesel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of 0.8 g/mL to 0.87 g/mL; (b) a sulfur content of 0.002 wt% or less; (c) a cetane index of 40 to 60; and (d) a kinematic viscosity at 50°C of 1.5 mm2/s to 4.0 mm2/s.
18. The blended fuel composition of claim 16, wherein the combination is the distillate fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein the blended fuel composition has one or more of the following properties: (a) a density of about 0.88 g/mL to about 1.1 g/mL; (b) a sulfur content of 3 wt% or less; (c ) a CCAl of about 750 to about 870; and (d) a kinematic viscosity at 5OC'C of about 5 mm2/s to about 700 mm2/s.
19. The blended fuel composition of claim 1 1, wherein the heavy pyrolysis fuel fraction of the plastic pyrolysis oil is the plastic pyrolysis total liquid product, and the heavy pyrolysis fuel fraction has one or more of the following properties: (a) a density of 0.70 g/mL to 0.90 g/mL; (b) a sulfur content of 150 ppm or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 3 mm2/s to 20 mm2/s.
20. The blended fuel composition of claim 19, wherein the combination is the heavy pyrolysis fuel fraction of the plastic pyrolysis total liquid product and the marine fuel, and wherein
the blended fuel composition has one or more of the following properties: (a) a density of 0.88 g/mL to 1.1 g/mL; (b) a sulfur content of 3 wt.% or less; (c) a CCAI of 750 to 870; and (d) a kinematic viscosity at 50°C of 5 mm2/s to 700 mm2/s.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US202163169388P | 2021-04-01 | 2021-04-01 | |
PCT/US2022/071191 WO2022213021A1 (en) | 2021-04-01 | 2022-03-17 | Blended fuel compositions including plastic pyrolysis oil and methods of making thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
EP4314198A1 true EP4314198A1 (en) | 2024-02-07 |
Family
ID=81327152
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP22714759.2A Pending EP4314198A1 (en) | 2021-04-01 | 2022-03-17 | Blended fuel compositions including plastic pyrolysis oil and methods of making thereof |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP4314198A1 (en) |
WO (1) | WO2022213021A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11884884B1 (en) | 2023-03-31 | 2024-01-30 | Nexus Circular LLC | Hydrocarbon compositions derived from pyrolysis of post-consumer and/or post-industrial plastics and methods of making and use thereof |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5997723A (en) | 1998-11-25 | 1999-12-07 | Exxon Research And Engineering Company | Process for blending petroleum oils to avoid being nearly incompatible |
US20080274022A1 (en) * | 2007-05-04 | 2008-11-06 | Boykin Jack W | Combined reactor and method for the production of synthetic fuels |
WO2020021104A1 (en) * | 2018-07-26 | 2020-01-30 | Yanchep Technology Limited | Production of fuel products from waste rubber material |
-
2022
- 2022-03-17 EP EP22714759.2A patent/EP4314198A1/en active Pending
- 2022-03-17 WO PCT/US2022/071191 patent/WO2022213021A1/en active Application Filing
Also Published As
Publication number | Publication date |
---|---|
WO2022213021A1 (en) | 2022-10-06 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1127100B1 (en) | Improved stability fischer-tropsch diesel fuel and a process for its production | |
US20190338205A1 (en) | Heavy Fuel Oil Product | |
JP4759138B2 (en) | Fischer-Tropsch diesel fuel production method with excellent stability | |
KR102024107B1 (en) | Systems and methods for renewable fuel | |
KR20220117901A (en) | Circular Economy of Plastic Waste to Polyethylene and Lubricants with Crude Oil and Isomerization Dewaxing Units | |
CN103189479B (en) | The production of recyclable organism distillate | |
EP4314198A1 (en) | Blended fuel compositions including plastic pyrolysis oil and methods of making thereof | |
KR20140096030A (en) | Process for the production of gasoline by using butanol in the gasoline pool | |
EP1950274A1 (en) | Light oil fuel | |
SK287556B6 (en) | Method for production motor fuels from polymer materials | |
AU2013292507A1 (en) | Process for producing biofuel using a pre-treated deoxygenated stream | |
Erawati et al. | Pyrolysis Process of Mixed Polypropylene (PP) and High-Density Polyethylene (HDPE) Waste with Natural Zeolite as Catalyst | |
CN103339232B (en) | By decon, in ebullated bed hydrocracking and the conversion by air distillation fractionation comprise the method for the hydrocarbon feed of shale oil | |
Jixing | Study on the conversion technology of waste polyethylene plastic to polyethylene wax | |
US6039771A (en) | Formulation and method of preparation of energy fortified diesel fuel | |
EP1613690A1 (en) | Method of obtaining high-quality products from polyolefine waste material or polyolefines | |
CN1487056A (en) | Method of raising liquid yield during delayed coking | |
FI20215816A1 (en) | Method of treating waste plastic | |
JP5676344B2 (en) | Kerosene manufacturing method | |
RU2235109C1 (en) | Bitumen production process | |
US20240117261A1 (en) | Method of producing a fuel oil including pyrolysis products generated from mixed waste plastics | |
KR100213986B1 (en) | Process for fuel by thermal decomposition waste of lubricating and waste plastics | |
JP4866579B2 (en) | Waste oil treatment method in oil refining | |
Adoga et al. | Catalytic pyrolysis of low density polyethylene and polypropylene wastes to fuel oils by N-clay | |
US3340178A (en) | Process for catalytically cracking pyrolysis condensates |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: UNKNOWN |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
17P | Request for examination filed |
Effective date: 20231020 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |