FI69694C - Nox-reduktion i multisolida svaevbaeddsfoerbraenningsanordningar - Google Patents

Nox-reduktion i multisolida svaevbaeddsfoerbraenningsanordningar Download PDF

Info

Publication number
FI69694C
FI69694C FI812631A FI812631A FI69694C FI 69694 C FI69694 C FI 69694C FI 812631 A FI812631 A FI 812631A FI 812631 A FI812631 A FI 812631A FI 69694 C FI69694 C FI 69694C
Authority
FI
Finland
Prior art keywords
particles
region
bed
combustion
fluidized bed
Prior art date
Application number
FI812631A
Other languages
English (en)
Finnish (fi)
Other versions
FI812631L (fi
FI69694B (fi
Inventor
Ke-Tien Liu
Herman Nack
Original Assignee
Battelle Development Corp
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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=22313021&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=FI69694(C) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by Battelle Development Corp filed Critical Battelle Development Corp
Publication of FI812631L publication Critical patent/FI812631L/fi
Publication of FI69694B publication Critical patent/FI69694B/fi
Application granted granted Critical
Publication of FI69694C publication Critical patent/FI69694C/fi

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/32Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with introduction into the fluidised bed of more than one kind of moving particles
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/54Nitrogen compounds
    • B01D53/56Nitrogen oxides
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/005Fluidised bed combustion apparatus comprising two or more beds
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/02Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
    • F23C10/04Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone
    • F23C10/08Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases
    • F23C10/10Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases the separation apparatus being located outside the combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2206/00Fluidised bed combustion
    • F23C2206/10Circulating fluidised bed
    • F23C2206/101Entrained or fast fluidised bed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C2206/00Fluidised bed combustion
    • F23C2206/10Circulating fluidised bed
    • F23C2206/103Cooling recirculating particles
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S423/00Chemistry of inorganic compounds
    • Y10S423/09Reaction techniques
    • Y10S423/16Fluidization

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Biomedical Technology (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Treating Waste Gases (AREA)
  • Catalysts (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Radar Systems Or Details Thereof (AREA)
  • Traffic Control Systems (AREA)

Claims (10)

1 Patentkrav
1. Sätt att sanka kväveoxidhalten till en önskad niva och minimera svaveldioxidhalten i förbränningsgaserna frln förbränning av bränsle 5 i en raed flera fasta ämnen arbetande svävbädd, som har en undre tät fluidiserad bädd med relativt Stora bäddpartiklar, en Övre dispergerad infangad bädd av relativt sett finare partiklar, vilka atermatas genom den tätare fluidiserade bädden, och ett däri infangat svavelsorptions-material, vid vilket 10 (A) ett nedre omrlde av svävbädden drives under stökiometriska förhallanden sa att NO sänkes tili den önskade nivan. x (B) ett övre omrlde av svävbädden ovanför det vid stökiometriska för-15 hlllanden drivna, undre omrldet drives vid oxiderande förhallanden för att fullständiga förbränningen av bränslet, känneteck-n a t därav, (C) att en kornstorleksskillnad upprätthälles mellan de relativt sett 20 större partiklarna och de relativt sett finare partiklarna, sa väsent- ligen alla av de förra partiklarna har atminstone 4 ggr sa stor korn-storlek som väsentligen alla de sistnämnda partiklarna och (D) att atminstone en del av de kylda, relativt sett finare partiklarna 25 atermatas fran den inflngade bädden genom väsentligen enbart det övre omrldet, som drives under oxiderande förhallanden, varigenom temperaturen i oxidationsomradet sänkes tili en niva, som befrämjar svavelinflngning medelst svavelsorptionsmaterialet. 30
2. Sätt enligt patentkravet 1, kännetecknat därav, att sekundärluften insprutas i förbränningsapparaten mellan det undre vid stökiometriska förhallanden drivna omrldet och det övre vid oxiderande förhallanden drivna omradet. 35
3. Sätt enligt patentkravet 2, kännetecknat därav, att extra sekundärluft inmatas i förbränningsapparaten inom det vid oxiderande förhallanden drivna omrldet.
FI812631A 1979-12-26 1981-08-26 Nox-reduktion i multisolida svaevbaeddsfoerbraenningsanordningar FI69694C (fi)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US06/106,745 US4704084A (en) 1979-12-26 1979-12-26 NOX reduction in multisolid fluidized bed combustors
US10674579 1979-12-26
PCT/US1980/001737 WO1981001873A1 (en) 1979-12-26 1980-12-22 No x reduction in multisolid fluidized bed combustors
US8001737 1980-12-22

Publications (3)

Publication Number Publication Date
FI812631L FI812631L (fi) 1981-08-26
FI69694B FI69694B (fi) 1985-11-29
FI69694C true FI69694C (fi) 1986-03-10

Family

ID=22313021

Family Applications (1)

Application Number Title Priority Date Filing Date
FI812631A FI69694C (fi) 1979-12-26 1981-08-26 Nox-reduktion i multisolida svaevbaeddsfoerbraenningsanordningar

Country Status (12)

Country Link
US (1) US4704084A (sv)
EP (2) EP0042418A1 (sv)
JP (1) JPS56501811A (sv)
AT (1) ATE12188T1 (sv)
BR (1) BR8009003A (sv)
CA (1) CA1156516A (sv)
DE (1) DE3070358D1 (sv)
DK (1) DK150285C (sv)
FI (1) FI69694C (sv)
NO (1) NO153746C (sv)
WO (1) WO1981001873A1 (sv)
ZA (1) ZA808096B (sv)

Families Citing this family (53)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1184743A (en) * 1981-10-09 1985-04-02 Herbert A. Arbib Superjet gas agitation process
US4453497A (en) * 1982-12-21 1984-06-12 Struthers Wells Corporation Augmented heat transfer method and apparatus
US5171542A (en) * 1984-03-20 1992-12-15 A. Ahlstrom Corporation Circulating fluidized bed reactor
US4672918A (en) * 1984-05-25 1987-06-16 A. Ahlstrom Corporation Circulating fluidized bed reactor temperature control
FI79403C (sv) * 1984-06-01 1989-12-11 Ahlstroem Oy Förbränningsmetod.
US4579070A (en) * 1985-03-01 1986-04-01 The M. W. Kellogg Company Reducing mode circulating fluid bed combustion
DK158531C (da) * 1985-06-13 1990-10-29 Aalborg Vaerft As Fremgangsmaade til kontinuerlig drift af en cirkulerende fluidiseret bed-reaktor samt reaktor til anvendelse ved udoevelse af fremgangsmaaden
FI853615L (fi) * 1985-09-20 1987-03-21 Tampella Oy Ab Foerfarande foer minskning av utslaeppen av kvaeve- och svaveloxider vid foerbraenning av kvaeve- och svavelhaltigt braensle.
FI86105C (sv) * 1985-11-19 1992-07-10 Ahlstroem Oy Förfarande och anordning för reglering av en virvelbäddsreaktors funkt ion
KR910001833B1 (ko) * 1985-12-09 1991-03-26 에이.아할스트롬 코포레이숀 순환 유동상 반응기(circulating fluidized bed reactor) 및 배기 가스로부터의 고체 물질 분리 방법
NO159879C (no) * 1986-05-02 1989-02-15 Santo As Fremgangsm te ved drift av et forbrenningsanlegg, segg for utfoerelse ten.
US4643110A (en) * 1986-07-07 1987-02-17 Enron, Inc. Direct fuel-fired furnace arrangement for the recovery of gallium and germanium from coal fly ash
DE3702089C1 (de) * 1987-01-24 1988-06-30 Kernforschungsanlage Juelich Wirbelschichtofen zur Muellverbrennung
DE3702892A1 (de) * 1987-01-31 1988-08-11 Rheinische Braunkohlenw Ag Verfahren und einrichtung zur behandlung von koernigen feststoffen in einer wirbelschicht
US4869207A (en) * 1987-07-13 1989-09-26 A. Ahlstrom Corporation Circulating fluidized bed reactor
FR2620517B1 (fr) * 1987-09-14 1989-12-22 Fives Cail Babcock Procede de combustion en lit fluidise et installation pour la mise en oeuvre de ce procede
US5141708A (en) * 1987-12-21 1992-08-25 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having an integrated recycle heat exchanger
FI87013C (sv) * 1988-01-04 1992-11-10 Tampella Oy Ab Bränningsförfarande för minskande av bildning av kväveoxider i samband med förbränning samt anordning för tillämpande av förfarandet
JP2637449B2 (ja) * 1988-01-12 1997-08-06 三菱重工業株式会社 流動床燃焼方法
US4881476A (en) * 1988-07-26 1989-11-21 The United States Of America As Represented By The United States Department Of Energy Cyclone reactor with internal separation and axial recirculation
US4927348A (en) * 1988-11-14 1990-05-22 Mobil Oil Corporation Circulating fluid bed combustion with CO combustion promoter and reduced combustion air
WO1991012465A1 (en) * 1988-11-14 1991-08-22 Mobil Oil Corporation Circulating fluid bed combustion with co combustion promoter
WO1991012464A1 (en) * 1988-11-14 1991-08-22 Mobil Oil Corporation Circulating fluid bed combustion with circulating co combustion promoter
US4899695A (en) * 1989-02-14 1990-02-13 Air Products And Chemicals, Inc. Fluidized bed combustion heat transfer enhancement
US5069170A (en) * 1990-03-01 1991-12-03 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having an integral recycle heat exchanger with inlet and outlet chambers
US5133943A (en) * 1990-03-28 1992-07-28 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having a multicompartment external recycle heat exchanger
US5054436A (en) * 1990-06-12 1991-10-08 Foster Wheeler Energy Corporation Fluidized bed combustion system and process for operating same
US5069171A (en) * 1990-06-12 1991-12-03 Foster Wheeler Agency Corporation Fluidized bed combustion system and method having an integral recycle heat exchanger with a transverse outlet chamber
FR2669099B1 (fr) * 1990-11-13 1994-03-18 Stein Industrie Procede et dispositif de combustion de materiaux carbones divises.
US5040492A (en) * 1991-01-14 1991-08-20 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having a recycle heat exchanger with a non-mechanical solids control system
US5140950A (en) * 1991-05-15 1992-08-25 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having an integral recycle heat exchanger with recycle rate control and backflow sealing
US5163374A (en) * 1991-08-27 1992-11-17 Institute Of Gas Technology Combustion process
FI91800C (sv) * 1991-09-12 1994-08-10 Imatran Voima Oy Förfarande och anordning vid avkylning av cirkulationsmassan i en svävväddspanna
WO1993018341A1 (en) * 1992-03-05 1993-09-16 Technische Universiteit Delft Method and apparatus for combusting a carbonaceous material
US5325796A (en) * 1992-05-22 1994-07-05 Foster Wheeler Energy Corporation Process for decreasing N2 O emissions from a fluidized bed reactor
US5239946A (en) * 1992-06-08 1993-08-31 Foster Wheeler Energy Corporation Fluidized bed reactor system and method having a heat exchanger
US5390612A (en) * 1993-03-01 1995-02-21 Foster Wheeler Energy Corporation Fluidized bed reactor having a furnace strip-air system and method for reducing heat content and increasing combustion efficiency of drained furnace solids
ZA946850B (en) * 1993-09-13 1995-04-21 Dorr Oliver Inc Firing liquid and gaseous fuels for a circulating fluidized bed reactor
US5735682A (en) * 1994-08-11 1998-04-07 Foster Wheeler Energy Corporation Fluidized bed combustion system having an improved loop seal valve
US5463968A (en) * 1994-08-25 1995-11-07 Foster Wheeler Energy Corporation Fluidized bed combustion system and method having a multicompartment variable duty recycle heat exchanger
TW419574B (en) * 1998-06-16 2001-01-21 Mitsubishi Heavy Ind Ltd Operating method of flow-level incinerator and the incinerator
US6089855A (en) * 1998-07-10 2000-07-18 Thermo Power Corporation Low NOx multistage combustor
DE10051733B4 (de) * 2000-10-18 2005-08-04 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Verfahren zur gestuften Verbrennung von Brennstoffen
US8449288B2 (en) * 2003-03-19 2013-05-28 Nalco Mobotec, Inc. Urea-based mixing process for increasing combustion efficiency and reduction of nitrogen oxides (NOx)
US7670569B2 (en) * 2003-06-13 2010-03-02 Mobotec Usa, Inc. Combustion furnace humidification devices, systems & methods
US7537743B2 (en) * 2004-02-14 2009-05-26 Mobotec Usa, Inc. Method for in-furnace regulation of SO3 in catalytic NOx reducing systems
US8251694B2 (en) * 2004-02-14 2012-08-28 Nalco Mobotec, Inc. Method for in-furnace reduction flue gas acidity
US7410356B2 (en) * 2005-11-17 2008-08-12 Mobotec Usa, Inc. Circulating fluidized bed boiler having improved reactant utilization
CN100491824C (zh) * 2007-11-02 2009-05-27 清华大学 低床压降循环流化床锅炉燃烧工艺方法
US8069824B2 (en) 2008-06-19 2011-12-06 Nalco Mobotec, Inc. Circulating fluidized bed boiler and method of operation
FI123853B (sv) * 2009-03-06 2013-11-15 Metso Power Oy Förfarande för minskning av kväveoxidutsläpp vid syreförbränning
FI125496B (sv) 2009-08-17 2015-10-30 Valmet Technologies Oy Förfarande och arrangemang för optimering av förbränningsförhållandena i en virvelbäddspanna
CN112426877B (zh) * 2020-09-24 2022-07-19 宣城市楷昂化工有限公司 一种焦亚硫酸钠生产中的氮氧化物废气的处理方法及其设备

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1181682B (de) * 1957-08-28 1964-11-19 Reinluft G M B H Verfahren zur Herstellung von Aktivkohle
US4033725A (en) * 1972-02-24 1977-07-05 John Zink Company Apparatus for NOx control using steam-hydrocarbon injection
DE2452717A1 (de) * 1974-11-06 1976-05-13 Nissan Motor Katalytisches konvertersystem fuer einen innenverbrennungsmotor
GB1488087A (en) * 1975-03-04 1977-10-05 Zink Co John Process for disposal of oxides of nitrogen
US4017272A (en) * 1975-06-05 1977-04-12 Bamag Verfahrenstechnik Gmbh Process for gasifying solid carbonaceous fuel
US4021184A (en) * 1975-10-02 1977-05-03 Dorr-Oliver Incorporated Dilute phase waste incinerator
GB1523500A (en) * 1975-10-21 1978-09-06 Battelle Development Corp Method of operating a fluidized bed system
DE2624302C2 (de) * 1976-05-31 1987-04-23 Metallgesellschaft Ag, 6000 Frankfurt Verfahren zur Durchführung exothermer Prozesse
US4103646A (en) * 1977-03-07 1978-08-01 Electric Power Research Institute, Inc. Apparatus and method for combusting carbonaceous fuels employing in tandem a fast bed boiler and a slow boiler
US4154581A (en) * 1978-01-12 1979-05-15 Battelle Development Corporation Two-zone fluid bed combustion or gasification process
US4158701A (en) * 1978-11-06 1979-06-19 Kaiser Aluminum & Chemical Corporation Pyrohydrolysis system for processing fluorine-containing spent and waste materials
DE2911712C2 (de) * 1979-03-24 1991-10-31 Bergwerksverband Gmbh, 4300 Essen Verfahren zur Entfernung von Schwefeloxiden und Stickstoffoxiden aus Abgasen

Also Published As

Publication number Publication date
CA1156516A (en) 1983-11-08
DE3070358D1 (en) 1985-04-25
EP0033808A1 (en) 1981-08-19
NO153746B (no) 1986-02-03
ATE12188T1 (de) 1985-04-15
EP0033808B1 (en) 1985-03-20
EP0042418A1 (en) 1981-12-30
DK375981A (da) 1981-08-25
ZA808096B (en) 1982-01-27
NO153746C (no) 1986-05-21
DK150285C (da) 1987-10-26
US4704084A (en) 1987-11-03
WO1981001873A1 (en) 1981-07-09
FI812631L (fi) 1981-08-26
NO812872L (no) 1981-08-25
FI69694B (fi) 1985-11-29
JPS56501811A (sv) 1981-12-10
DK150285B (da) 1987-01-26
BR8009003A (pt) 1981-10-20

Similar Documents

Publication Publication Date Title
FI69694C (fi) Nox-reduktion i multisolida svaevbaeddsfoerbraenningsanordningar
US5105747A (en) Process and apparatus for reducing pollutant emissions in flue gases
US5133950A (en) Reducing N2 O emissions when burning nitrogen-containing fuels in fluidized bed reactors
EP0770198B1 (en) Combustion method
CA1292148C (en) Method and system for controlling the backflow sealing efficiency and recycle rate in fluidized bed reactors
US5043150A (en) Reducing emissions of N2 O when burning nitrogen containing fuels in fluidized bed reactors
US4308810A (en) Apparatus and method for reduction of NOx emissions from a fluid bed combustion system through staged combustion
US4597774A (en) Method for improving the operation of a fluidized bed
US7004089B2 (en) Combined fluidized bed and pulverized coal combustion method
JP3317496B2 (ja) N2o排出物の減少
CN102483231A (zh) 用于优化流化床锅炉中的燃烧条件的方法和装置
KR930023058A (ko) 유동층 반응기로부터 일산화이질소(n_2o) 방출을 감소시키는 방법
WO1993018341A1 (en) Method and apparatus for combusting a carbonaceous material
SU663963A1 (ru) Способ сжигани топлива
JP3095499B2 (ja) 流動層燃焼ボイラ
US6415743B2 (en) Method of decreasing nitrogen oxide emissions in a circulating fluidized bed combustion system
AU6704581A (en) No x reduction in multisolid fluidized bed combustors
Findlay et al. How to reduce pollutant emissions from small fluidised-bed combustors
GB2104796A (en) Reduction of NOx emission from fluidized bed combustion systems
Gulyurtlu et al. Co-combustion of forestry biomass with tyres in a circulating fluidised bed combustor
JPH074624A (ja) 煙道ガス中の放出汚染物質を減少する方法と装置
JPH05296429A (ja) 流動床燃焼装置

Legal Events

Date Code Title Description
PC Transfer of assignment of patent

Owner name: INTERNATIONAL PAPER COMPANY

MM Patent lapsed
MM Patent lapsed

Owner name: INTERNATIONAL PAPER COMPANY