US2013205727A1PendingUtilityA1
Devices and Methods for a Pyrolysis and Gasification System for Biomass Feedstock
Individually held — no corporate assignee on recordPriority: Feb 5, 2010Filed: Feb 7, 2011Published: Aug 15, 2013
Est. expiryFeb 5, 2030(~3.5 yrs left)· nominal 20-yr term from priority
C10G 2/32F23G 2201/40F23J 2217/40C10J 3/84F23C 10/20C10K 1/026F23G 2203/501C10J 2200/15C10J 2300/0916Y02P20/145F23G 5/30F23G 7/10B04C 5/26C10J 3/482F23C 10/10C10J 3/503B01J 8/44C10J 2300/0956F23G 5/027C10J 3/54G01F 13/001C10B 53/00F23C 10/00C10G 1/02Y10T137/85938G01F 1/76C10K 1/32F16L 41/02Y02E50/10C10B 49/22C10J 3/463C10B 53/02Y02E50/30
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Claims
Abstract
A pyrolysis and gasification system and method convert a biomass feed stock to bio-char and synthesis gas. In one embodiment, the pyrolysis and gasification system includes a reactor for producing a synthesis gas and bio-char from a biomass feedstock. The system includes a flow measurement device and an air distribution system, which provides a fluidized bed in the reactor. The system also includes a cyclone assembly. The cyclone assembly removes the bio-char from the synthesis gas.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . An air distribution system for a reactor, wherein bed materials are disposed in the reactor, comprising:
an air distribution plate; a plurality of air distributors, wherein the plurality of air distributors are attached to the air distribution plate; wherein each of the air distributors comprises a base and a distribution arm, and wherein the distribution arm comprises distributor orifices; and wherein the distribution arm is disposed about parallel to the air distribution plate, and wherein the distribution arm comprises a bottom side, and further wherein the distributor orifices are disposed on the bottom side of the distribution arm.
2 . The air distribution system of claim 1 , wherein the air distribution system provides air to the bed materials to provide a fluidized bed in the reactor.
3 . The air distribution system of claim 2 , wherein the air distribution system is submerged in the fluidized bed.
4 . The air distribution system of claim 1 , wherein the reactor is disposed in a gasifier for producing a synthesis gas and bio-char from a biomass feedstock.
5 . The air distribution system of claim 1 , wherein the distribution arm is disposed about perpendicular to the base.
6 . The air distribution system of claim 1 , wherein air flows from the base to the distribution arm.
7 . A flow measurement device adapted for measuring biomass flow, comprising:
a plurality of feed rollers, wherein each of the feed rollers is rotatable, and wherein each feed roller comprises a roller shaft and roller blades; and wherein the flow measurement device is calibrated to allow determination of the biomass flow from rotation of the feed rollers.
8 . The flow measurement device of claim 7 , wherein the roller blades of a feed roller contact the roller blades of an adjacent feed roller when one or both of the feed rollers are rotating.
9 . The flow measurement device of claim 7 , further comprising a metering device attached to each feed roller.
10 . The flow measurement device of claim 9 , wherein rotation of each feed roller rotates the attached metering device.
11 . The flow measurement device of claim 9 , wherein the metering device comprises metering device ridges and contact points disposed between each adjacent metering device ridge.
12 . The flow measurement device of claim 11 , wherein a metering device ridge is disposed in the contact point of an adjacent metering device.
13 . The flow measurement device of claim 9 , wherein each metering device rotates with rotation of an adjacent metering device.
14 . A cyclone assembly for removing char from a gas produced from a biomass feedstock, comprising:
a first cyclone, wherein the first cyclone is a low energy cyclone; a second cyclone, wherein the second cyclone is a high efficiency cyclone; and wherein the first cyclone is disposed to receive the gas, and wherein the gas exiting the first cyclone flows to the second cyclone.
15 . The cyclone assembly of claim 14 , wherein the gas comprises a temperature, and wherein the first cyclone and the second cyclone are operated at about the temperature of the gas.
16 . The cyclone assembly of claim 14 , wherein the gas flows to the second cyclone through a cyclone duct.
17 . The cyclone assembly of claim 14 , wherein the first cyclone is a 1D1D cyclone, and wherein the second cyclone is a 1D3D cyclone.
18 . The cyclone assembly of claim 14 , wherein the first cyclone is a 1D3D cyclone, and wherein the second cyclone is a 1D5D cyclone.
19 . The cyclone assembly of claim 14 , wherein the first cyclone and/or the second cyclone comprise a rotary air lock.
20 . The cyclone assembly of claim 14 , wherein the first cyclone comprises a cut-point of about 6 micrometers aerodynamic equivalent diameter, and the second cyclone comprises a cut-point of about 3 micrometers aerodynamic equivalent diameter.Join the waitlist — get patent alerts
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