Method and apparatus for processing biomass material

• US 9,127,227 B2
• Filed: 09/14/2012
• Issued: 09/08/2015
• Est. Priority Date: 09/16/2011
• Status: Active Grant

• Current Assignee: Astec (SK Hynix Inc.)
• Original Assignee: Astec (SK Hynix Inc.)
• Inventors: Brock, J. Donald, Swanson, Malcolm L., Catlett, Gary L., Pruett, Jeffrey Blake
• Primary Examiner(s): MCAVOY, ELLEN M
• Application Number:
  US13/616,184
• Publication Number:
  US 20130067806A1
• Time in Patent Office: 1,089 Days
• Field of Search: 445/89, 446/29, 446/35, 446/36
• US Class Current: 1/1
• CPC Class Codes: C10L 5/363 Pellets or granulates
• CPC Class Codes: C10L 5/44 on vegetable substances
• 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

Abstract

An assembly for processing green biomass material for pelletizing into a fuel pellet includes a heating assembly, a drying assembly and a cooling assembly. The heating assembly heats a thermal fluid to a temperature within the range of 200° F. to 550° F. The drying assembly includes a rotating dryer drum that has a plurality of thermal fluid tubes therein. Material that is dried in the dryer drum is conveyed to a rotating cooling drum that has a cooling tube extending along the interior thereof. A nozzle is mounted on the end of the cooling tube to discharge cooling fluid on the material therein, and a plurality of flights are mounted on the interior of the cooling drum and arranged to direct material from the inlet to the discharge outlet as the cooling drum is rotated.

Claims

1. A method for making a fuel pellet from biomass, said method comprising:

(A) providing a heating assembly comprising;

(1) a burner;

(2) a heat exchanger having a plurality of heat transfer coils therein;

(3) a combustion chamber that is operatively connected between the burner and the heat exchanger so that the burner may be operated to heat a thermal fluid in the heat transfer coils to a temperature within the range of 200°

F. to 550°

F.;

(B) providing a drying assembly comprising;

(1) a dryer frame having;

(a) an upper end;

(b) a lower end;

(2) a generally cylindrical dryer drum that is mounted on the dryer frame for rotation about the axis of the dryer drum, said dryer drum having;

(a) an upper end having an inlet;

(b) a lower end having a discharge outlet;

(c) a plurality of thermal fluid tubes extending along the interior thereof;

(3) means for rotating the dryer drum with respect to the dryer frame;

(4) means for conveying the thermal fluid from the heat exchanger of the heating assembly through the thermal fluid tubes in the dryer drum;

(C) providing a cooling assembly comprising;

(1) a cooler frame;

(2) a generally cylindrical cooling drum that is mounted on the cooler frame for rotation about the axis of the cooling drum, said cooling drum having;

(a) an inlet end having an inlet;

(b) an outlet end having a discharge outlet;

(c) a cooling tube extending along the interior thereof;

(d) a nozzle mounted on the cooling tube so as to discharge cooling fluid into the interior of the cooling drum;

(e) a plurality of flights mounted on the interior of the cooling drum and arranged to direct material from the inlet end to the outlet end as the cooling drum is rotated;

(3) means for rotating the cooling drum with respect to the cooler frame;

(4) means for conveying cooling fluid through the cooling tube;

(D) providing a steam duct for conveying steam from the upper end of dryer drum to the combustion chamber;

(E) providing a VOC duct for conveying volatile organic compounds from the lower end of the dryer drum to the combustion chamber;

(F) providing a pellet press for compressing white biomass or torrefied biomass;

(G) introducing green biomass into the inlet at the upper end of the dryer drum;

(H) operating the burner to heat thermal fluid in the heat exchanger, without causing such thermal fluid to undergo a change of phase, to a temperature of at least about 200°

F. if it is desired to produce white biomass, or operating the burner to heat thermal fluid in the heat exchanger, without causing such thermal fluid to undergo a change of phase, to a temperature within the range of about 475°

F. to about 550°

F. if it is desired to produce torrefied biomass;

(I) conveying heated thermal fluid from the heat exchanger through the thermal fluid tubes in the drum dryer;

(J) rotating the drum dryer at a rate sufficient to convey the green biomass introduced into the inlet thereof to the discharge outlet of the dryer drum as it is heated to a temperature of at least about 200°

F. so as to convert the green biomass into white biomass, or rotating the dryer drum at a rate sufficient to convey the green biomass introduced into the inlet thereof to the discharge outlet of the dryer drum as it is heated to a temperature of at least about 475°

F. so as to convert the green biomass into torrefied biomass;

(K) conveying the white biomass or torrefied biomass from the discharge outlet of the dryer drum to the inlet of the cooling drum;

(L) conveying cooling fluid through the cooling tube of the cooling drum so that it is discharged through the nozzle of the cooling drum onto the white biomass or torrefied biomass therein;

(M) rotating the cooling drum at a rate sufficient to convey the white biomass or torrefied biomass introduced into the inlet thereof to the discharge outlet of the cooling drum as it is cooled to a temperature that is less than about 150°

F.;

(N) conveying the white biomass or the torrefied biomass to the pellet press;

(O) operating the pellet press to compress the white biomass or the torrefied biomass to produce fuel pellets.

2. The method of claim 1 which includes operating the pellet press to compress the white biomass material or the torrefied biomass material at a pressure of about 10,000 psi in a die heated to a temperature within the range of about 500°

F. to about 530°

F. for a period of at least about one second.

3. The method of claim 1 which includes the step of rotating the cooling drum at a rate sufficient to convey the white biomass or torrefied biomass introduced into the inlet thereof to the discharge outlet of the cooling drum as it is cooled to a temperature that is less than about 130°

F.

4. The method of claim 1 which includes:

(A) providing a recirculation system to recirculate gases from the exhaust of the heat exchanger to the dryer drum, said recirculation system comprising;

(1) an outlet line from the heat exchanger;

(2) an inlet line to the dryer drum; and

(3) a recirculating fan that is in fluid communication with the outlet line from the heat exchanger and the inlet line to the dryer drum;

(B) operating the recirculating fan to draw gases from the exhaust of the heat exchanger and transport said gases to the dryer drum.

5. The method of claim 1 which includes:

(A) providing a predryer for heating green biomass material, said predryer comprising;

(1) an inclined rotating predryer drum, said drum having;

(a) an upper end;

(b) a lower end;

(c) a long axis;

(d) a rotation system for rotating the predryer drum about its long axis;

(2) an inlet chute for green biomass material located at the upper end of the predryer drum;

(3) a gas inlet line for exhaust gases from the heat exchanger located at the upper end of the predryer drum, so that hot flue gases from the heat exchanger are directed into the predryer drum so as to flow therethrough parallel to the flow of biomass;

(4) an outlet for pre-dried biomass located at the lower end of the predryer drum;

(5) a conveyor located at the lower end of the predryer drum for transporting pre-dried biomass to the dryer drum;

(B) operating the rotation system to rotate the predryer drum about its long axis;

(C) introducing green biomass material into the inlet chute of the predryer drum;

(D) directing hot flue gases from the heat exchanger into the gas inlet line to predryer drum so as to flow therethrough parallel to the flow of biomass therein;

(E) discharging pre-dried biomass from the outlet of the predryer drum.

6. The method of claim 5 which includes:

(A) conveying the pre-dried biomass from the outlet of the predryer drum to the inlet of the drum dryer;

(B) rotating the drum dryer at a rate sufficient to convey the pre-dried biomass introduced into the inlet thereof to the discharge outlet of the dryer drum as it is heated to a temperature sufficient to convert the pre-dried biomass into torrefied biomass having a heating value within the range of about 8900 BTU/lb to about 9500 BTU/lb.

7. The method of claim 1:

(A) which includes providing an external fuel supply to the burner;

(B) which includes means for controlling the supply of external fuel to the burner;

(C) supplying external fuel to the burner at a first rate;

(D) adjusting the rate of supply of external fuel to the burner to a second rate that is lower than the first rate, as volatile organic compounds obtained from heating the green biomass in the dryer drum are conveyed from the lower end of the dryer drum to the combustion chamber.