WO2013011281A4 - Improvements in Waste Processing - Google Patents

Improvements in Waste Processing Download PDF

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Publication number
WO2013011281A4
WO2013011281A4 PCT/GB2012/051648 GB2012051648W WO2013011281A4 WO 2013011281 A4 WO2013011281 A4 WO 2013011281A4 GB 2012051648 W GB2012051648 W GB 2012051648W WO 2013011281 A4 WO2013011281 A4 WO 2013011281A4
Authority
WO
WIPO (PCT)
Prior art keywords
gas
conveying
processing tube
tube
section
Prior art date
Application number
PCT/GB2012/051648
Other languages
French (fr)
Other versions
WO2013011281A2 (en
WO2013011281A3 (en
Inventor
Rifat Al Chalabi
Ophneil Henry Perry
John Turner
Original Assignee
Chinook End-Stage Recycling Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chinook End-Stage Recycling Limited filed Critical Chinook End-Stage Recycling Limited
Priority to EA201400148A priority Critical patent/EA201400148A1/en
Priority to CN201280045813.1A priority patent/CN103814117B/en
Priority to EP12740641.1A priority patent/EP2734606A2/en
Priority to MX2014000691A priority patent/MX2014000691A/en
Priority to US14/233,460 priority patent/US20140284197A1/en
Priority to JP2014520718A priority patent/JP2014523811A/en
Priority to AU2012285548A priority patent/AU2012285548A1/en
Priority to CA2845794A priority patent/CA2845794A1/en
Priority to BR112014001059A priority patent/BR112014001059A2/en
Publication of WO2013011281A2 publication Critical patent/WO2013011281A2/en
Publication of WO2013011281A3 publication Critical patent/WO2013011281A3/en
Publication of WO2013011281A4 publication Critical patent/WO2013011281A4/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/08Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated in dispersed form
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65FGATHERING OR REMOVAL OF DOMESTIC OR LIKE REFUSE
    • B65F5/00Gathering or removal of refuse otherwise than by receptacles or vehicles
    • B65F5/005Gathering or removal of refuse otherwise than by receptacles or vehicles by pneumatic means, e.g. by suction
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/002Horizontal gasifiers, e.g. belt-type gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/06Continuous processes
    • C10J3/14Continuous processes using gaseous heat-carriers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02Fixed-bed gasification of lump fuel
    • C10J3/20Apparatus; Plants
    • C10J3/22Arrangements or dispositions of valves or flues
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • F23G5/0273Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage using indirect heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B17/00Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
    • F26B17/10Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by fluid currents, e.g. issuing from a nozzle, e.g. pneumatic, flash, vortex or entrainment dryers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/12Heating the gasifier
    • C10J2300/1253Heating the gasifier by injecting hot gas

Abstract

M&C PB143543WO 22 31524653-1-abhimani ABSTRACT An apparatus and method for processing organic materials is provided comprising an elongate process tube (22) having an inlet for receiving the material and an outlet for processed material. A gas conveying system fluidically conveys the material through the processing tube, The gas conveying system comprises a supply of conveying gas which is a hot pressurised inert gas, connected to the processing tube (22) at its inlet end. A control system is configured to control the supply of the pressurised inert gas to the processing tube (22) so as to convey a batch of material through the tube (22) whilst simultaneously heating said it to cause the organic matter therein to gasify to produce process. The processing tube (22) has a plurality of sections, each separated by a closure (44), and the gas conveying means conveys the material from one section to the next. (Figure 1)

Claims

AMENDED CLAIMS
received by the International Bureau on 26 March 2013 (26.03.2013)
CLAIMS:
1 Apparatus for processing material such as organically coated waste and organic materials including biomass, industrial waste, municipal solid waste and sludge; the apparatus comprising:
an elongate process tube having an inlet for receiving the material and an outlet for processed material;
a gas conveying system for fluidically conveying said material through said processing tube, said conveying system comprising a supply of conveying gas, comprising hot pressurised inert gas, connected to said processing tube at its inlet end; and
a control system configured to control the supply of said pressurised inert gas to said processing tube so as to convey a batch of said material through said tube simultaneously heating said material to cause any organic matter therein to gasify to produce process gas wherein
the processing tube comprises a plurality of sections, each separated by a valve, and wherein the gas conveying means is configured to convey the material from one section to the next. 2 The apparatus of claim 1 further comprising separation means for extracting the process gas from the processing tube.
3 The apparatus of claim 1 or claim 2 wherein the gas conveying means includes a conveying gas inlet associated with each section for the supply of conveying gas to move the material therein into the next section.
4 The apparatus of any one of the preceding claims further comprising a conveying gas compressor for increasing the pressure of the conveying gas and wherein expansion of the conveying gas moves the material in the processing tube.
5 The apparatus of claim 4 wherein the conveying gas compressor comprises a compression chamber having a piston therein for receiving said conveying gas and an actuator for moving said piston in said chamber to compress the gas therein. 6 The apparatus of claim 5 wherein the compression chamber is sized such that one stroke of the piston in the chamber expels sufficient conveying gas to convey material from one section of the processing tube to be to another. 7 The apparatus according to claim 4 or claim 6 wherein each section of the processing tube has a compressor associated with it.
8 The apparatus according to any one of the preceding claims further comprising a fluid outlet in each section of the tube for draining fluid therefrom.
9 The apparatus according to claim 5 further comprising a fluid outlet in each section of the tube for draining fluid therefrom and a fluid inlet in the conveying gas inlet conduit of each section for feeding fluid into said conveying gas. 10 The apparatus of any preceding claim further comprising at least one thermal treatment chamber for thermally treating the process gas produced by the apparatus by heating it so as to breakdown any volatile organic compounds therein.
11 The apparatus according to claim 10 further comprising an outlet conduit from at least one thermal treatment chamber for supplying hot process gas therefrom to the processing tube for use as said conveying gas.
12 The apparatus according to any previous claim further comprising: a feed hopper for receiving and temporarily storing material to be processed, and a secondary hopper fed by the feed hopper wherein the secondary hopper is connected to the processing tube by a valve and wherein the secondary hopper has a conveying gas inlet at an upper end thereof.
13 The apparatus according to any previous claim wherein each section of the processing tube has a process gas outlet towards its downstream end.
14 The apparatus according to any previous claim further comprising sensors to sense the quality of the process gas and: if it does not meet a predetermined criteria, recirculating the process gas through the processing tube and, if it does meet the predetermined criteria extracting at least a part of the process gasses for storage or direct use.
15 The apparatus according to any previous claim wherein the interior surface of the processing tube is provided with fixed agitators to promote the tumbling of material within said tube as it is conveyed therethrough.
16 A method for processing material such as organically coated waste and organic materials including biomass, industrial waste, municipal solid waste and sludge; the method comprising:
providing an elongate process tube having an inlet for receiving the material and an outlet for processed material;
providing a gas conveying system for fluidically conveying said material through said processing tube, said conveying system comprising a supply of hot pressurised inert gas connected to said processing tube at its inlet end; and
controlling the supply of said pressurised inert gas to said processing tube so as to convey a batch of said material through said tube thereby heating said material to cause any organic matter therein to gasify to produce process gas wherein
the processing tube comprises a plurality of sections, each separated by a valve, each section having a conveying gas inlet associated therewith for the supply of conveying gas; the method further comprising controlling the supply of conveying gas so as to convey the material from one section to the next.
17 The method of claim 16 further comprising separating the process gas from the processing tube.
18 The method of claim 17 further comprising compressing the conveying gas to increase its pressure and wherein expansion of the conveying gas moves the material in the processing tube.
19 The method of any one of claims 16 to 18 further comprising draining fluid from each section of the tube via a fluid outlet therein.
20 The method according to claim 19 further comprising supplying fluid drained from the tube into the conveying gas upstream of the processing tube. 21 The method according to claim 20 wherein the temperature of the conveying gas is sufficient to vaporise the fluid added thereto, thereby increasing the pressure of said conveying gas.
22 The method any one of claims 16 to 21 further comprising heating the process gases in a thermal treatment chamber to thermally breakdown any volatile organic compounds therein. 23 The method according to claim 22 further comprising supplying hot process gas from the thermal treatment chamber to the processing tube for use as said conveying gas.
24 The method according to any one of claims 16 to 23 further comprising: providing a feed hopper for receiving and temporarily storing material to be processed; providing a secondary hopper fed by the feed hopper wherein the secondary hopper is connected to the processing tube by a valve; providing a conveying gas inlet at an upper end of the secondary hopper; feeding a batch of material to be processed from the feed hopper to the secondary hopper; passing gas through the conveying gas inlet and opening the valve such that the batch of material is conveyed from the secondary hopper into the processing tube..
25 The method according to any one of claims 16 to 24 further comprising providing each section of the processing tube with a process gas outlet towards its downstream end and extracting process gas via said process gas outlets.
26 The method according to any one of claims 16 to 25 further comprising sensing the quality of the process gas and: if it does not meet a predetermined criteria, recirculating the process gas through the processing tube and, if it does meet the predetermined criteria extracting at least a part of the process gasses for storage or direct use.
27 The method according to any one of claims 16 to 25 further comprising providing a waste material silo downstream of the processing tube for collecting the inert fully processed material 28 The method according to any one of claims 16 to 27 further comprising agitating said material within the tube as it is conveyed there through. 29 The method according to claim 16 further comprising heating the process gases from initial sections of the processing tube in a first thermal treatment chamber, to thermally breakdown any volatile organic compounds therein, and recycling the treated gas as conveying gas. 30 The method of claim 29 further comprising heating the process gases from final sections of the processing tube in a second thermal treatment chamber, to thermally breakdown any volatile organic compounds therein.
31 The method of claim 16 further comprising determining the quality of the process gas and: if the process gas is below a predetermined quality threshold, passing the process gas through a first thermal treatment chamber to heat the gas so as to thermally breakdown any volatile organic compounds therein, and recycling the treated gas as conveying gas; and if the process gas is above a predetermined quality threshold, passing the process gas through a second thermal treatment chamber to heat the gas so as to thermally breakdown any volatile organic compounds therein.
PCT/GB2012/051648 2011-07-20 2012-07-12 Improvements in Waste Processing WO2013011281A2 (en)

Priority Applications (9)

Application Number Priority Date Filing Date Title
EA201400148A EA201400148A1 (en) 2011-07-20 2012-07-12 IMPROVING WASTE TREATMENT
CN201280045813.1A CN103814117B (en) 2011-07-20 2012-07-12 The improvement of refuse process
EP12740641.1A EP2734606A2 (en) 2011-07-20 2012-07-12 Improvements in Waste Processing
MX2014000691A MX2014000691A (en) 2011-07-20 2012-07-12 Improvements in Waste Processing.
US14/233,460 US20140284197A1 (en) 2011-07-20 2012-07-12 Waste Processing
JP2014520718A JP2014523811A (en) 2011-07-20 2012-07-12 Improved waste treatment
AU2012285548A AU2012285548A1 (en) 2011-07-20 2012-07-12 Improvements in waste processing
CA2845794A CA2845794A1 (en) 2011-07-20 2012-07-12 Improvements in waste processing
BR112014001059A BR112014001059A2 (en) 2011-07-20 2012-07-12 waste processing improvements

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1112503.6A GB2493004B (en) 2011-07-20 2011-07-20 Method and apparatus for gasifying organic materials
GB1112503.6 2011-07-20

Publications (3)

Publication Number Publication Date
WO2013011281A2 WO2013011281A2 (en) 2013-01-24
WO2013011281A3 WO2013011281A3 (en) 2013-04-18
WO2013011281A4 true WO2013011281A4 (en) 2013-06-06

Family

ID=44586911

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB2012/051648 WO2013011281A2 (en) 2011-07-20 2012-07-12 Improvements in Waste Processing

Country Status (13)

Country Link
US (1) US20140284197A1 (en)
EP (1) EP2734606A2 (en)
JP (1) JP2014523811A (en)
CN (1) CN103814117B (en)
AU (1) AU2012285548A1 (en)
BR (1) BR112014001059A2 (en)
CA (1) CA2845794A1 (en)
CL (1) CL2014000132A1 (en)
EA (1) EA201400148A1 (en)
GB (1) GB2493004B (en)
MX (1) MX2014000691A (en)
TW (1) TW201313346A (en)
WO (1) WO2013011281A2 (en)

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Also Published As

Publication number Publication date
EA201400148A1 (en) 2014-06-30
GB201112503D0 (en) 2011-08-31
TW201313346A (en) 2013-04-01
CN103814117A (en) 2014-05-21
CL2014000132A1 (en) 2014-11-21
WO2013011281A2 (en) 2013-01-24
MX2014000691A (en) 2014-07-30
JP2014523811A (en) 2014-09-18
CN103814117B (en) 2015-09-02
CA2845794A1 (en) 2013-01-24
US20140284197A1 (en) 2014-09-25
AU2012285548A1 (en) 2014-03-06
EP2734606A2 (en) 2014-05-28
WO2013011281A3 (en) 2013-04-18
GB2493004A (en) 2013-01-23
BR112014001059A2 (en) 2017-02-21
GB2493004B (en) 2013-08-21

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