Processing materials

• US 9,644,244 B2
• Filed: 08/19/2016
• Issued: 05/09/2017
• Est. Priority Date: 10/10/2012
• Status: Active Grant

• Current Assignee: Xyleco, Inc.
• Original Assignee: Xyleco, Inc.
• Inventors: Medoff, Marshall, Masterman, Thomas Craig, Paradis, Robert
• Primary Examiner(s): Vanore, David A
• Application Number:
  US15/241,965
• Publication Number:
  US 20160358744A1
• Time in Patent Office: 263 Days
• Field of Search: 2504923, 2504921, 250397, 25045311, 25045511, 2503631, 2504961, 20415763, 20415715, 2041573, 20415768
• CPC Class Codes: A61L 2/087 Particle radiation, e.g. electron-beam, alpha or beta radiation
• CPC Class Codes: B01J 19/082 Gamma-radiation only
• CPC Class Codes: B01J 19/085 Electron beams only
• CPC Class Codes: B01J 19/12 employing electromagnetic waves
• CPC Class Codes: B01J 19/123 Ultraviolet light
• CPC Class Codes: B01J 19/125 X-rays
• CPC Class Codes: B01J 19/22 in the form of endless belts
• CPC Class Codes: B01J 2219/0869 Feeding or evacuating the reactor
• CPC Class Codes: B01J 2219/0871 Heating or cooling of the reactor
• CPC Class Codes: B01J 2219/0879 Solid
• CPC Class Codes: B01J 2219/12 Processes employing electromagnetic waves
• CPC Class Codes: B01J 2219/1203 Incoherent waves
• CPC Class Codes: B65G 27/04 Load carriers other than helical or spiral channels or conduits
• CPC Class Codes: C08H 8/00 Macromolecular compounds derived from lignocellulosic materials pretreatment thereof B27N
• CPC Class Codes: C10B 19/00 Heating of coke ovens by electrical means
• CPC Class Codes: C10B 53/02 of cellulose-containing material production of pyroligneous acid C10C5/00
• CPC Class Codes: C10G 1/02 by distillation
• CPC Class Codes: C10G 32/04 by particle radiation
• CPC Class Codes: C10L 2200/0469 Renewables or materials of biological origin
• CPC Class Codes: C10L 2290/24 Mixing, stirring of fuel components
• CPC Class Codes: C10L 2290/28 : Cutting, disintegrating, shredding or grinding
• CPC Class Codes: C10L 2290/36 : Applying radiation such as microwave, IR, UV
• CPC Class Codes: C10L 2290/52 : Hoppers
• CPC Class Codes: C10L 5/403 : on paper and paper waste
• CPC Class Codes: C10L 5/442 : Wood or forestry waste
• CPC Class Codes: C10L 5/445 : Agricultural waste, e.g. corn crops, grass clippings, nut shells or oil pressing residues
• CPC Class Codes: C10L 5/46 : on sewage, house, or town refuse C10L5/403, C10L5/406 take precedence
• CPC Class Codes: C12P 2201/00 : Pretreatment of cellulosic or lignocellulosic material for subsequent enzymatic treatment or hydrolysis
• CPC Class Codes: C12P 7/10 : substrate containing cellulosic material
• CPC Class Codes: C13K 1/02 : obtained by saccharification of cellulosic materials manufacture of fodder A23K10/32
• CPC Class Codes: C13K 13/002 : Xylose
• CPC Class Codes: D21B 1/02 : Pretreatment of the raw materials by chemical or physical means removal of bark B27L
• CPC Class Codes: G21F 3/00 : Shielding characterised by its physical form, e.g. granules, or shape of the material
• CPC Class Codes: G21K 5/04 : with beam-forming means
• CPC Class Codes: G21K 5/10 : with provision for relative movement of beam source and object to be irradiated
• CPC Class Codes: H01J 2237/2002 : Controlling environment of sample
• CPC Class Codes: H01J 2237/202 : Movement
• CPC Class Codes: H01J 33/04 : Windows
• CPC Class Codes: H01J 37/20 : Means for supporting or positioning the object or the material; Means for adjusting diaphragms or lenses associated with the support
• CPC Class Codes: H01J 37/317 : for changing properties of the objects or for applying thin layers thereon, e.g. for ion implantation H01J37/36 takes precedence
• CPC Class Codes: H01J 5/18 : Windows permeable to X-rays, gamma-rays, or particles
• CPC Class Codes: Y02E 50/10 : Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 : Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02P 20/145 : the feedstock being materials of biological origin
• CPC Class Codes: Y02P 60/87 : Re-use of by-products of food processing for fodder production

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 to an electron beam while conveying the biomass material on a conveyor, and cooling a surface of the conveyor.

2. The method of claim 1, wherein the conveyer is a vibratory conveyor.

3. The method of claim 2, wherein the vibratory conveyor comprises a vibratory conveyor trough conveying the biomass.

4. The method of claim 3, wherein the vibratory conveyor trough comprises a first surface of the vibratory conveyor trough conveying the biomass, and cooling comprises cooling a second surface of the vibratory conveyor trough by contacting the second surface with a cooling enclosure containing a cooling fluid, wherein the first and second surfaces of the vibratory conveyor trough are in thermal communication.

5. The method of claim 4, wherein the distance between the first and second surface of the vibratory conveyor trough is between about 1/64 and 2 inches.

6. The method of claim 4, wherein the second surface of the vibratory conveyor trough forms a part of the cooling enclosure.

7. The method of claim 4, 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 agent from the inlet to the outlet.

9. The method of claim 7, further comprising maintaining a difference in the temperature of the cooling agent at the inlet of the cooling enclosure to the temperature at the outlet of the enclosure of between about 2 to 120°

C.

10. The method of claim 6, further comprising maintaining a flow rate of cooling fluid through the cooling enclosure of between 0.5 and 150 gallons/minute.