Biomass gasification/pyrolysis system and process

Abstract

A system and process capable of promoting the energy content of a syngas produced from a biomass material. The system and process entail compacting a loose biomass material and simultaneously introducing the compacted biomass material into an entrance of a reactor tube, and then heating the compacted biomass material within the tube to a temperature at which organic molecules within the biomass material break down to form ash and a fuel gas mixture. The fuel gas mixture is withdrawn from the tube and the ash is removed from the tube through an exit thereof. The entrance and exit of the tube, the compaction step, and the removal step cooperate to inhibit ingress of air into the tube by forming a plug of the biomass material at the entrance of the tube and a plug of ash at the exit of the tube.

1 . A system for producing syngas from biomass materials, the system comprising:
 a reactor containing a reactor tube having an internal passage, an entrance to the internal passage, and an exit to the internal passage;   means for compacting a loose biomass material and simultaneously introducing the compacted biomass material into the entrance of the reactor tube;   means for heating the compacted biomass material within the reactor tube to a temperature at which organic molecules within the compacted biomass material break down to form ash and a fuel gas mixture comprising carbon monoxide and hydrogen gases;   means for withdrawing the fuel gas mixture from the reactor tube;   means for removing the ash from the reactor tube through the exit thereof; and   means comprising the compacting means, the entrance and the exit of the reactor tube, and the removing means for inhibiting ingress of air into the reactor tube by sufficiently compacting the biomass material at the entrance of the reactor tube to form a plug of the compacted biomass material at the entrance and compacting the ash at the exit of the reactor tube to form a plug of the ash at the exit.   
     
     
         2 . The system according to  claim 1 , wherein the inhibiting means further comprises:
 means for monitoring pressures at the entrance and the exit of the reactor tube; and   means for monitoring and adjusting a volumetric rate of the fuel gas mixture withdrawn from the reactor tube by the withdrawing means based on the pressures at the entrance and the exit of the reactor tube.   
     
     
         3 . The system according to  claim 1 , wherein the reactor tube comprises first and second heating zones through which the biomass material travels in sequence through the reactor tube, and the second heating zone is at a higher temperature than the first heating zone. 
     
     
         4 . The system according to  claim 1 , further comprising means for injecting a gasification agent into the reactor tube. 
     
     
         5 . The system according to  claim 4 , wherein the gasification agent is steam. 
     
     
         6 . The system according to  claim 4 , wherein the reactor tube comprises first and second heating zones through which the biomass material travels in sequence through the reactor tube, the second heating zone is at a higher temperature than the first heating zone, and the gasification agent is introduced into the second heating zone within the reactor tube. 
     
     
         7 . The system according to  claim 1 , wherein the compacting means comprises a hopper containing a quantity of the biomass material. 
     
     
         8 . The system according to  claim 7 , wherein the compacting means comprises an auger that transports the biomass material from the hopper to the entrance of the reactor tube. 
     
     
         9 . The system according to  claim 1 , wherein the entrance of the reactor tube is flared to promote compaction of the biomass material within the entrance. 
     
     
         10 . The system according to  claim 1 , wherein the removing means comprises a manifold that tapers to promote compaction of the ash within the exit of the reactor tube. 
     
     
         11 . A process of producing syngas from biomass materials and performed with the system of  claim 1 , the process comprising:
 compacting the loose biomass material and simultaneously introducing the compacted biomass material into the entrance of the reactor tube;   heating the compacted biomass material within the reactor tube to a temperature at which organic molecules within the compacted biomass material break down to form the ash and the fuel gas mixture;   withdrawing the fuel gas mixture from the reactor tube;   removing the ash from the reactor tube through the exit thereof; and   inhibiting ingress of air into the reactor tube by sufficiently compacting the biomass material at the entrance of the reactor tube to form the plug of the compacted biomass material at the entrance and compacting the ash at the exit of the reactor tube to form the plug of the ash at the exit.   
     
     
         12 . A process of producing syngas from biomass materials, the process comprising:
 compacting a loose biomass material and simultaneously introducing the compacted biomass material into an entrance of a reactor tube;   heating the compacted biomass material within the reactor tube to a temperature at which organic molecules within the compacted biomass material break down to form ash and a fuel gas mixture comprising carbon monoxide and hydrogen gases;   withdrawing the carbon monoxide and hydrogen gases from the reactor tube;   removing the ash from the reactor tube through an exit thereof; and   inhibiting ingress of air into the reactor tube by sufficiently compacting the biomass material at the entrance of the reactor tube to form a plug of the compacted biomass material at the entrance and compacting the ash at the exit of the reactor tube to form a plug of the ash at the exit.   
     
     
         13 . The process according to  claim 12 , wherein the inhibiting step further comprises:
 monitoring pressures at the entrance and the exit of the reactor tube; and   monitoring and adjusting a volumetric rate of the fuel gas mixture withdrawn from the reactor tube based on the pressures at the entrance and the exit of the reactor tube.   
     
     
         14 . The process according to  claim 12 , wherein the biomass material travels in sequence through first and second heating zones within the reactor tube, and the second heating zone is at a higher temperature than the first heating zone. 
     
     
         15 . The process according to  claim 12 , further comprising injecting a gasification agent into the reactor tube. 
     
     
         16 . The process according to  claim 15 , wherein the gasification agent is steam. 
     
     
         17 . The process according to  claim 15 , wherein the biomass material travels in sequence through first and second heating zones within the reactor tube, the second heating zone is at a higher temperature than the first heating zone, and the gasification agent is introduced into the second heating zone within the reactor tube. 
     
     
         18 . The process according to  claim 12 , wherein the compacting step comprises transporting the biomass material from a hopper to the entrance of the reactor tube. 
     
     
         19 . The process according to  claim 12 , wherein the entrance of the reactor tube is flared to promote compaction of the biomass material within the entrance. 
     
     
         20 . The process according to  claim 12 , wherein the ash removed from the reactor tube enters a manifold that is tapered to promote compaction of the ash within the exit of the reactor tube.