METHOD AND SYSTEM FOR ROASTING A BIOMASS FEEDSTOCK

• US 20090193679A1
• Filed: 06/28/2007
• Published: 08/06/2009
• Est. Priority Date: 06/29/2006
• Status: Abandoned Application

• Current Assignee: Guyomarc'H, Raymond
• Original Assignee: Guyomarc'H, Raymond
• Inventors: Guyomarc'h, Raymond
• Application Number:
  US12/306,839
• Publication Number:
  US 20090193679A1
• Time in Patent Office: Days
• US Class Current: 34/467
• CPC Class Codes: C10B 53/02 of cellulose-containing material production of pyroligneous acid C10C5/00
• CPC Class Codes: C10L 5/44 on vegetable substances
• CPC Class Codes: C10L 9/083 Torrefaction
• CPC Class Codes: F23G 7/105 of wood waste
• CPC Class Codes: Y02E 20/12 Heat utilisation in combustion or incineration of waste
• 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

Abstract

A method for roasting a load of plant biomass, includes the following stages: generation of a treatment gas stream by a thermal generating apparatus, the treatment gas stream being an inert gas consisting essentially of CO₂; generation of a bed of material at high temperature, called the thermal base; treatment of the load of biomass with the treatment gas stream, the treatment gas stream being laden with gaseous components including a water steam and volatile organic compounds originating from the load of biomass during the treatment; and recycling of at least a portion of the water steam by passing at least a portion of the laden gas stream through the thermal base.

Claims

1-53. -53. (canceled)

54. A method for roasting a load of plant biomass, comprising the following stages:

generation of a treatment gas stream by thermal generating means, said treatment gas stream being an inert gas consisting essentially of CO₂;

generation of a bed of material at high temperature, called the thermal base;

treatment of said load of biomass with said treatment gas stream, said treatment gas stream being laden with gaseous components comprising water steam and volatile organic compounds originating from said load of biomass during said treatment; and

recycling of at least a portion of said water steam by passing at least a portion of said laden gas stream through said thermal base.

55. The method according to claim 54, characterized in that the reactive thermal base is essentially composed of carbon-containing constituents at high temperature obtained by combustion under O₂ of dried biomass.

56. The method according to claim 54, characterized in that the thermal base is burning at a temperature that is controlled by injection of oxygen in the center of said base.

57. The method according to claim 54, characterized in that it additionally comprises combustion, during passage of the laden gas stream through the thermal base, of organic gaseous components originating from the load of biomass and present in said laden gas stream, said combustion producing thermal energy that can be used directly in the method and/or electric power by means of dedicated systems.

58. The method according to claim 54, characterized in that it further comprises recycling of the laden gas stream to recover the gas that can be used in the treatment gas stream, said recycling comprising a filtering of the laden gas stream, after the passage of said stream through the thermal base.

59. The method according to claim 54, characterized in that the generation of the gas stream for roasting comprises:

a combustion of roasted biomass under O₂, said combustion producing a combustion gas consisting essentially of CO₂, and

a condensation of H₂O components contained in the combustion gas, in order to recover a residual gas consisting essentially of carbon dioxide CO₂.

60. The method according to claim 59, characterized in that the residual gas travels through at least one heat exchanger to acquire the treatment temperature, and then is returned to the treatment cycle, to be used in the treatment of the load of biomass to be roasted, the thermal energy necessary for raising the residual gas to the treatment temperature is obtained by combustion of dried biomass.

61. The method according to claim 54, characterized in that the treatment gas stream is generated by combustion of a solid fuel, said combustion also generating at least a portion of the thermal base.

62. A system for roasting a load of plant biomass, comprising:

generating means provided for generating an inert treatment gas stream consisting essentially of CO₂ and a bed of material at high temperature, called the thermal base;

a treatment unit, provided for receiving and subjecting said load of biomass to said treatment gas stream, said treatment unit comprising a treatment furnace and means for feeding the load of biomass into said treatment furnace and for removing said load of biomass from said treatment furnace; and

gas exchange means provided for communication between the generating means and the treatment unit.

63. The system according to claim 62, characterized in that the generating means comprise a thermal generator provided for generating:

at least a portion of the treatment gas stream, and

at least a portion of the thermal base

said generator comprising a thermal reactor or a solid-fuel furnace or alternatively a hybrid device, allowing the combustion of a solid fuel and a gaseous fuel.

64. The system according to claim 63, characterized in that the thermal generator is equipped with a system for cooling by circulation of a heat-transfer fluid.

65. The system according to claim 63, characterized in that the thermal generator comprises a grate-type furnace provided for receiving the thermal base and arranged for effecting the transfer of the laden gases originating from the treatment unit.

66. The system according to claim 63, characterized in that the thermal generator comprises means for injecting oxygen.

67. The system according to claim 63, characterized in that the thermal generator comprises a chamber for post-combustion of pyrolysis gases generated by the roasting of the load of biomass and/or by the incomplete combustion of a solid fuel.

68. The system according to claim 63, characterized in that the thermal generator comprises at least one heat exchanger, said heat exchanger being provided for effecting heat exchange between either a combustion gas and the treatment gas stream, or a fluid composed essentially of saturated water steam and the treatment gas stream, said fluid being essentially composed of water steam originating either from the roasting of the load of biomass or from a cooling circuit of a part of said system.

69. The system according to claim 62, characterized in that the furnace is a cylindrical assembly comprising an inner cylinder housed in an outer cylinder defining a space for treatment of the load of biomass, said inner cylinder being provided with freedom to rotate about a longitudinal axis relative to the outer cylinder and receiving the load of plant biomass to be roasted.

70. The system according to claim 69, characterized in that the inner cylinder comprises an inside wall which is perforated and at least one protuberance on said inside wall, said protuberance ensuring entrainment and mixing of the load of biomass during the treatment.

71. The system according to claim 69, characterized in that the outer cylinder has a heat-insulated shell and a solid inside wall enveloping the inner cylinder and delimiting the treatment space of the biomass feed.

72. The system according to claim 69, characterized in that the treatment furnace comprises a deflector on almost the entire length of the cylinder intended for directing the treatment gas stream towards the lower portion of the treatment space so as to distribute said stream onto all of the load of biomass.

73. The system according to claim 69, characterized in that the treatment furnace has at least two brushes mounted in contact on the one hand with the inside wall of the outer cylinder and on the other hand between the outside wall of the inner cylinder so as to delimit a zone for feed of the treatment gas stream into the treatment furnace and a zone for extracting the gas stream after treatment of the load of biomass, said brushes being arranged for brushing the outside wall of the inner cylinder so as to dislodge particles of the load of biomass clinging to the inner cylinder.

74. The system according to claim 69, characterized in that the treatment unit further comprises driving means arranged for providing rotation of the inner cylinder about a longitudinal axis.

75. The system according to claim 69, characterized in that one end of the inner cylinder and of the outer cylinder is provided with an opening permitting introduction of the load of biomass into the inner cylinder before the treatment and extraction of said load of biomass after the treatment, the other end being closed, said opening being tightly closed by sealing means actuated by piston means.

76. The system according to claim 69, characterized in that:

in a position called the charging position, the cylindrical assembly is positioned vertically, the end having an opening in the inner cylinder and outer cylinder that is at the top, in such a way that the load of biomass to be treated can be fed into the inner cylinder,

in a position called the process position, the cylindrical assembly is positioned horizontally, the opening of the inner cylinder and outer cylinder is tightly closed by the sealing means, and

in a position called the discharging position, the cylindrical assembly is positioned vertically, the end having an opening of the inner cylinder and outer cylinder that is positioned at the bottom, in such a way that the load of biomass treated is collected in receiving means.

77. The system according to claim 69, characterized in that it further comprises means for extracting the gas mixture from the treatment space, provided so that said treatment space is kept at a slight low pressure.