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Patent · US10163535B2 · B2 · US

Processing materials

(11) Publication number
US10163535B2
(21) Application number
15/703,887
(22) Filing date
2017-09-13
(30) Priority date
2012-10-10
(43) Publication date
2018-12-25
(45) Date of grant
2018-12-25
(51) IPC
A61L 2/08; B01J 19/08; B01J 19/12; B01J 19/22; B65G 27/04; C08H 8/00; C10B 19/00; C10B 53/02; C10G 1/02; C10G 32/04; C10L 5/40; C10L 5/44; C10L 5/46; C13K 1/02; C13K 13/00; D21B 1/02; G21F 3/00; G21K 5/04; G21K 5/10; H01J 33/04; H01J 37/20; H01J 37/317; H01J 5/18
(52) CPC
  • B01J Chemical or physical processes, e.g. catalysis or colloid chemistry; their relevant apparatus: 19/085, 19/082, 19/12, 19/123, 19/125, 19/22, 2219/0869, 2219/0871, 2219/0879, 2219/12, 2219/1203
  • A61L Methods or apparatus for sterilising materials or objects in general; disinfection, sterilisation or deodorisation of air; chemical aspects of bandages, dressings, absorbent pads or surgical articles; materials for bandages, dressings, absorbent pads or surgical articles: 2/087
  • B65G Transport or storage devices, e.g. conveyors for loading or tipping, shop conveyor systems or pneumatic tube conveyors: 27/04
  • C08H Derivatives of natural macromolecular compounds: 8/00
  • C10B Destructive distillation of carbonaceous materials for production of gas, coke, tar, or similar materials: 19/00, 53/02
  • 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: 1/02, 32/04
  • C10L Fuels not otherwise provided for; natural gas; synthetic natural gas obtained by processes not covered by subclasses C10G or C10K; liquified petroleum gas; use of additives to fuels or fires; fire-lighters: 2200/0469, 2290/24, 2290/28, 2290/36, 2290/52, 5/403, 5/442, 5/445, 5/46
  • C12P Fermentation or enzyme-using processes to synthesise a desired chemical compound or composition or to separate optical isomers from a racemic mixture {}: 2201/00, 7/10
  • C13K Saccharides obtained from natural sources or by hydrolysis of naturally occurring disaccharides, oligosaccharides or polysaccharides: 1/02, 13/002
  • D21B Fibrous raw materials or their mechanical treatment: 1/02
  • G21F Protection against x-radiation, gamma radiation, corpuscular radiation or particle bombardment; treating radioactively contaminated material; decontamination arrangements therefor: 3/00
  • G21K Handling of particles or ionising radiation not otherwise provided for; irradiation devices; gamma ray or x-ray microscopes: 5/04, 5/10
  • H01J Electric discharge tubes or discharge lamps: 2237/2002, 2237/202, 33/04, 37/20, 37/317, 5/18
  • Y02E Reduction of greenhouse gas [ghg] emissions, related to energy generation, transmission or distribution: 50/10, 50/14, 50/16, 50/30, 50/32
  • Y02P Climate change mitigation technologies in the production or processing of goods: 20/145, 60/87
(73) Assignee
XYLECO INC
(72) Inventors
MEDOFF MARSHALL; MASTERMAN THOMAS CRAIG; PARADIS ROBERT
(54) Title
Processing materials
(57) Abstract

Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful intermediates and products, such as energy, fuels, foods or materials. For example, systems and methods are described that can be used to treat feedstock materials, such as cellulosic and/or lignocellulosic materials, while cooling equipment and the biomass to prevent overheating and possible distortion and/or degradation. The biomass is conveyed by a conveyor, which conveys the biomass under an electron beam from an electron beam accelerator. The conveyor can be cooled with cooling fluid. The conveyor can also vibrate to facilitate exposure to the electron beam. The conveyor can be configured as a trough that can be optionally cooled.

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Claims (22)

  1. A method of conveying a material under an electron beam, the method comprising: exposing a biomass material having a bulk density of less than 0.7 g/cm 3 to an electron beam while conveying the biomass material on a vibratory conveyor, wherein the biomass material is treated with electron bombardment having energies of 0.5-10 MeV via the electron beam, wherein the vibratory conveyor comprises a vibratory conveyor trough, wherein the vibratory conveyor trough comprises a first surface of the vibratory conveyor trough conveying the biomass, and the method further comprises cooling a second surface of the vibratory conveyor trough, wherein the first and second surfaces of the vibratory conveyor trough are in thermal communication.
  2. The method of claim 1, wherein the total electron beam power has at least 50 kW of power.
  3. The method of claim 1, wherein the vibratory conveyor comprises a metal, alloys of metals or coated and alloys of metals.
  4. The method of claim 1, wherein the distance between the first and second surface of the vibratory conveyor trough is between 0.0396875 and 5.08 cm (1/64 and 2 inches).
  5. The method of claim 1, further comprising cooling the second surface by contacting the second surface with a cooling enclosure containing a cooling fluid.
  6. The method of claim 5, wherein the second surface of the vibratory conveyor trough forms a part of the cooling enclosure.
  7. The method of claim 5, further comprising flowing fluid through the cooling enclosure by flowing the cooling fluid into the cooling enclosure through an inlet to the enclosure and flowing the fluid out of the cooling enclosure through an outlet from the cooling enclosure.
  8. The method of claim 7, wherein the cooling enclosure comprises channels configured to allow the flow of the cooling fluid from the inlet to the outlet.
  9. The method of claim 7, further comprising maintaining a difference in the temperature of the cooling fluid at the inlet of the cooling enclosure to the temperature at the outlet of the enclosure of between 2 to 120° C.
  10. The method of claim 5, further comprising maintaining a flow rate of cooling fluid through the cooling enclosure of between 1.8925 and 567.75 liters/minute (0.5 and 150 gallons/minute).
  11. A method of conveying a material under an electron beam, the method comprising: exposing a biomass material having a bulk density of less than 0.7 g/cm 3 to an electron beam from a scan horn while conveying the biomass material on a vibratory conveyor, wherein the biomass material is treated with electron bombardment having energies of 0.5-10 MeV via the electron beam, and wherein the vibratory conveyor is oscillated in a direction parallel to the direction of conveying and perpendicular to the scan horn of the electron beam.
  12. The method of claim 11 where the vibratory conveyor comprises a vibratory conveyor trough conveying the biomass.
  13. The method of claim 12 wherein vibratory conveyor trough comprises a first surface of the vibratory conveyor trough conveying the biomass, and the method further comprises cooling a second surface of the vibratory conveyor trough, wherein the first and second surfaces of the vibratory conveyor trough are in thermal communication.
  14. The method of claim 11, wherein the total electron beam power has at least 50 kW of power.
  15. The method of claim 11, wherein the vibratory conveyor comprises a metal, alloys of metals or coated and alloys of metals.
  16. The method of claim 13, wherein the distance between the first and second surface of the vibratory conveyor trough is between 0.0396875 and 5.08 cm (1/64 and 2 inches).
  17. The method of claim 13, further comprising cooling the second surface by contacting the second surface with a cooling enclosure containing a cooling fluid.
  18. The method of claim 17, wherein the second surface of the vibratory conveyor trough forms a part of the cooling enclosure.
  19. The method of claim 17, further comprising flowing fluid through the cooling enclosure by flowing the cooling fluid into the cooling enclosure through an inlet to the enclosure and flowing the fluid out of the cooling enclosure through an outlet from the cooling enclosure.
  20. The method of claim 19, wherein the cooling enclosure comprises channels configured to allow the flow of the cooling fluid from the inlet to the outlet.
  21. The method of claim 19, further comprising maintaining a difference in the temperature of the cooling fluid at the inlet of the cooling enclosure to the temperature at the outlet of the enclosure of between 2 to 120° C.
  22. The method of claim 17, further comprising maintaining a flow rate of cooling fluid through the cooling enclosure of between 1.8925 and 567.75 liters/minute (0.5 and 150 gallons/minute).

Description

This application is a continuation application of U.S. patent application Ser. No. 15/472,985, filed Mar. 29, 2017, which is a continuation application of U.S. patent application Ser. No. 15/241,965, filed Aug. 19, 2016, now U.S. Pat. No. 9,644,244, granted on May 9, 2017, which is a continuation application of U.S. patent application Ser. No. 15/195,206, filed Jun. 28, 2016, now U.S. Pat. No. 9,455,118, granted on Sep. 27, 2016, which is a continuation application of U.S. patent application Ser. No. 14/435,026, filed Apr. 10, 2015, now U.S. Pat. No. 9,435,076, granted on Sep. 6, 2016, which is a National Stage of International Application No. PCT/US2013/064320 filed on Oct. 10, 2013, which claims the benefit of U.S. Provisional Application No. 61/711,801, filed on Oct. 10, 2012; 61/711,807, filed on Oct. 10, 2012; 61/774,684, filed on Mar. 8, 2013; 61/774,773, filed on Mar. 8, 2013; 61/774,731, filed on Mar. 8, 2013; 61/774,735, filed on Mar. 8, 2013; 61/774,744, filed on Mar. 8, 2013; 61/774,746, filed on Mar. 8, 2013; 61/774,750, filed on Mar. 8, 2013; 61/774,752, filed on Mar. 8, 2013; 61/774,754, filed on Mar. 8, 2013; 61/774,775, filed on Mar. 8, 2013; 61/774,780, filed on Mar. 8, 2013; 61/774,761, filed on Mar. 8, 2013; 61/774,723, filed on Mar. 8, 2013, all of which are hereby incorporated by reference in their entireties.

Many potential lignocellulosic feedstocks are available today, including agricultural residues, woody biomass, municipal waste, oilseeds/cakes and seaweed, to name a few.

Citations (91)

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Record as JSON
{
  "publication_number": "US10163535B2",
  "country": "US",
  "kind": "B2",
  "title": "Processing materials",
  "abstract": "Biomass (e.g., plant biomass, animal biomass, and municipal waste biomass) is processed to produce useful intermediates and products, such as energy, fuels, foods or materials. For example, systems and methods are described that can be used to treat feedstock materials, such as cellulosic and/or lignocellulosic materials, while cooling equipment and the biomass to prevent overheating and possible distortion and/or degradation. The biomass is conveyed by a conveyor, which conveys the biomass under an electron beam from an electron beam accelerator. The conveyor can be cooled with cooling fluid. The conveyor can also vibrate to facilitate exposure to the electron beam. The conveyor can be configured as a trough that can be optionally cooled.",
  "claims": [
    "1. A method of conveying a material under an electron beam, the method comprising: exposing a biomass material having a bulk density of less than 0.7 g/cm 3 to an electron beam while conveying the biomass material on a vibratory conveyor, wherein the biomass material is treated with electron bombardment having energies of 0.5-10 MeV via the electron beam, wherein the vibratory conveyor comprises a vibratory conveyor trough, wherein the vibratory conveyor trough comprises a first surface of the vibratory conveyor trough conveying the biomass, and the method further comprises cooling a second surface of the vibratory conveyor trough, wherein the first and second surfaces of the vibratory conveyor trough are in thermal communication.",
    "2. The method of claim 1, wherein the total electron beam power has at least 50 kW of power.",
    "3. The method of claim 1, wherein the vibratory conveyor comprises a metal, alloys of metals or coated and alloys of metals.",
    "4. The method of claim 1, wherein the distance between the first and second surface of the vibratory conveyor trough is between 0.0396875 and 5.08 cm (1/64 and 2 inches).",
    "5. The method of claim 1, further comprising cooling the second surface by contacting the second surface with a cooling enclosure containing a cooling fluid.",
    "6. The method of claim 5, wherein the second surface of the vibratory conveyor trough forms a part of the cooling enclosure.",
    "7. The method of claim 5, further comprising flowing fluid through the cooling enclosure by flowing the cooling fluid into the cooling enclosure through an inlet to the enclosure and flowing the fluid out of the cooling enclosure through an outlet from the cooling enclosure.",
    "8. The method of claim 7, wherein the cooling enclosure comprises channels configured to allow the flow of the cooling fluid from the inlet to the outlet.",
    "9. The method of claim 7, further comprising maintaining a difference in the temperature of the cooling fluid at the inlet of the cooling enclosure to the temperature at the outlet of the enclosure of between 2 to 120° C.",
    "10. The method of claim 5, further comprising maintaining a flow rate of cooling fluid through the cooling enclosure of between 1.8925 and 567.75 liters/minute (0.5 and 150 gallons/minute).",
    "11. A method of conveying a material under an electron beam, the method comprising: exposing a biomass material having a bulk density of less than 0.7 g/cm 3 to an electron beam from a scan horn while conveying the biomass material on a vibratory conveyor, wherein the biomass material is treated with electron bombardment having energies of 0.5-10 MeV via the electron beam, and wherein the vibratory conveyor is oscillated in a direction parallel to the direction of conveying and perpendicular to the scan horn of the electron beam.",
    "12. The method of claim 11 where the vibratory conveyor comprises a vibratory conveyor trough conveying the biomass.",
    "13. The method of claim 12 wherein vibratory conveyor trough comprises a first surface of the vibratory conveyor trough conveying the biomass, and the method further comprises cooling a second surface of the vibratory conveyor trough, wherein the first and second surfaces of the vibratory conveyor trough are in thermal communication.",
    "14. The method of claim 11, wherein the total electron beam power has at least 50 kW of power.",
    "15. The method of claim 11, wherein the vibratory conveyor comprises a metal, alloys of metals or coated and alloys of metals.",
    "16. The method of claim 13, wherein the distance between the first and second surface of the vibratory conveyor trough is between 0.0396875 and 5.08 cm (1/64 and 2 inches).",
    "17. The method of claim 13, further comprising cooling the second surface by contacting the second surface with a cooling enclosure containing a cooling fluid.",
    "18. The method of claim 17, wherein the second surface of the vibratory conveyor trough forms a part of the cooling enclosure.",
    "19. The method of claim 17, further comprising flowing fluid through the cooling enclosure by flowing the cooling fluid into the cooling enclosure through an inlet to the enclosure and flowing the fluid out of the cooling enclosure through an outlet from the cooling enclosure.",
    "20. The method of claim 19, wherein the cooling enclosure comprises channels configured to allow the flow of the cooling fluid from the inlet to the outlet.",
    "21. The method of claim 19, further comprising maintaining a difference in the temperature of the cooling fluid at the inlet of the cooling enclosure to the temperature at the outlet of the enclosure of between 2 to 120° C.",
    "22. The method of claim 17, further comprising maintaining a flow rate of cooling fluid through the cooling enclosure of between 1.8925 and 567.75 liters/minute (0.5 and 150 gallons/minute)."
  ],
  "description_excerpt": "This application is a continuation application of U.S. patent application Ser. No. 15/472,985, filed Mar. 29, 2017, which is a continuation application of U.S. patent application Ser. No. 15/241,965, filed Aug. 19, 2016, now U.S. Pat. No. 9,644,244, granted on May 9, 2017, which is a continuation application of U.S. patent application Ser. No. 15/195,206, filed Jun. 28, 2016, now U.S. Pat. No. 9,455,118, granted on Sep. 27, 2016, which is a continuation application of U.S. patent application Ser. No. 14/435,026, filed Apr. 10, 2015, now U.S. Pat. No. 9,435,076, granted on Sep. 6, 2016, which is a National Stage of International Application No. PCT/US2013/064320 filed on Oct. 10, 2013, which claims the benefit of U.S. Provisional Application No. 61/711,801, filed on Oct. 10, 2012; 61/711,807, filed on Oct. 10, 2012; 61/774,684, filed on Mar. 8, 2013; 61/774,773, filed on Mar. 8, 2013; 61/774,731, filed on Mar. 8, 2013; 61/774,735, filed on Mar. 8, 2013; 61/774,744, filed on Mar. 8, 2013; 61/774,746, filed on Mar. 8, 2013; 61/774,750, filed on Mar. 8, 2013; 61/774,752, filed on Mar. 8, 2013; 61/774,754, filed on Mar. 8, 2013; 61/774,775, filed on Mar. 8, 2013; 61/774,780, filed on Mar. 8, 2013; 61/774,761, filed on Mar. 8, 2013; 61/774,723, filed on Mar. 8, 2013, all of which are hereby incorporated by reference in their entireties.\n\nMany potential lignocellulosic feedstocks are available today, including agricultural residues, woody biomass, municipal waste, oilseeds/cakes and seaweed, to name a few.",
  "cpc": [
    "B01J 19/085",
    "A61L 2/087",
    "B01J 19/082",
    "B01J 19/12",
    "B01J 19/123",
    "B01J 19/125",
    "B01J 19/22",
    "B01J 2219/0869",
    "B01J 2219/0871",
    "B01J 2219/0879",
    "B01J 2219/12",
    "B01J 2219/1203",
    "B65G 27/04",
    "C08H 8/00",
    "C10B 19/00",
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    "C10L 2290/24",
    "C10L 2290/28",
    "C10L 2290/36",
    "C10L 2290/52",
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    "C10L 5/445",
    "C10L 5/46",
    "C12P 2201/00",
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  ],
  "assignees": [
    "XYLECO INC"
  ],
  "inventors": [
    "MEDOFF MARSHALL",
    "MASTERMAN THOMAS CRAIG",
    "PARADIS ROBERT"
  ],
  "filing_date": "2017-09-13",
  "publication_date": "2018-12-25",
  "grant_date": "2018-12-25",
  "priority_date": "2012-10-10",
  "application_number": "US-201715703887-A",
  "family_id": "50477883",
  "citations": [
    "JP2000254486A",
    "JP2000304900A",
    "JP2001242297A",
    "JP2001318200A",
    "JP2003153987A",
    "JP2010008387A",
    "JP2012011382A",
    "JPH11169438A",
    "JPH11337700A",
    "US1525035A",
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    "US1962573A",
    "US2008210718A1",
    "US2010087687A1",
    "US2010112242A1",
    "US2011081335A1",
    "US2011111456A1",
    "US2011262985A1",
    "US2012237984A1",
    "US2012315675A1",
    "US2014209093A1",
    "US2014243444A1",
    "US2014284203A1",
    "US2014286714A1",
    "US2015265999A1",
    "US2015284907A1",
    "US2015287487A1",
    "US2016053047A1",
    "US2016201152A1",
    "US2016358744A1",
    "US2017197194A1",
    "US2017221679A1",
    "US2017275463A1",
    "US2018036706A1",
    "US2144382A",
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    "US2566316A",
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