NO20020111D0 - Partikkelseparator - Google Patents

Partikkelseparator

Info

Publication number
NO20020111D0
NO20020111D0 NO20020111A NO20020111A NO20020111D0 NO 20020111 D0 NO20020111 D0 NO 20020111D0 NO 20020111 A NO20020111 A NO 20020111A NO 20020111 A NO20020111 A NO 20020111A NO 20020111 D0 NO20020111 D0 NO 20020111D0
Authority
NO
Norway
Prior art keywords
gas
particles
separated
bed reactor
reactor system
Prior art date
Application number
NO20020111A
Other languages
English (en)
Other versions
NO20020111L (no
Inventor
Lennart Ahlgren
Erik Rensfelt
Original Assignee
Tps Termiska Processer Ab
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 Tps Termiska Processer Ab filed Critical Tps Termiska Processer Ab
Publication of NO20020111D0 publication Critical patent/NO20020111D0/no
Publication of NO20020111L publication Critical patent/NO20020111L/no

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/005—Separating solid material from the gas/liquid stream
    • B01J8/0065—Separating solid material from the gas/liquid stream by impingement against stationary members
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical 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
    • B01J8/38—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/386—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical 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
    • B01J8/38—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/388—Chemical 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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00—Fluidised bed combustion apparatus
    • F23C10/02—Fluidised 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
    • F23C10/04—Fluidised 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
    • F23C10/08—Fluidised 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00548—Flow

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Cyclones (AREA)
  • Acyclic And Carbocyclic Compounds In Medicinal Compositions (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Details Of Garments (AREA)
NO20020111A 1999-07-15 2002-01-09 Partikkelseparator NO20020111L (no)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE9902711A SE522657C2 (sv) 1999-07-15 1999-07-15 Förfarande och reaktorsystem för avskiljande av partiklar från en gas
PCT/SE2000/001478 WO2001006178A1 (en) 1999-07-15 2000-07-11 Particle separator

Publications (2)

Publication Number Publication Date
NO20020111D0 true NO20020111D0 (no) 2002-01-09
NO20020111L NO20020111L (no) 2002-03-14

Family

ID=20416508

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20020111A NO20020111L (no) 1999-07-15 2002-01-09 Partikkelseparator

Country Status (11)

Country Link
US (1) US6743280B1 (no)
EP (1) EP1196719B1 (no)
AT (1) ATE297529T1 (no)
AU (1) AU767945B2 (no)
CA (1) CA2379164A1 (no)
CZ (1) CZ2002101A3 (no)
DE (1) DE60020709D1 (no)
NO (1) NO20020111L (no)
PL (1) PL352496A1 (no)
SE (1) SE522657C2 (no)
WO (1) WO2001006178A1 (no)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8410504B2 (en) 2008-06-10 2013-04-02 Koninklijke Philips Electronics N.V. LED module
CZ2010541A3 (cs) * 2010-07-09 2011-08-24 Novopol A.S. Zpusob trídení a zarízení k jeho uskutecnení
CN114471385B (zh) * 2022-02-14 2023-04-28 聊城市鲁西化工工程设计有限责任公司 一种聚式流化有机硅合成反应控制方法和装置

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4253425A (en) 1979-01-31 1981-03-03 Foster Wheeler Energy Corporation Internal dust recirculation system for a fluidized bed heat exchanger
FI66297C (fi) * 1982-11-15 1984-10-10 Ahlstroem Oy Anordning foer avlaegsnande av fasta komponenter ur roekgaser
US4712514A (en) 1986-09-05 1987-12-15 Qinghua University Fluidized bed boiler and high temperature separators used therein
DE3640377A1 (de) 1986-11-26 1988-06-09 Steinmueller Gmbh L & C Verfahren zur verbrennung von kohlenstoffhaltigen materialien in einem wirbelschichtreaktor und vorrichtung zur durchfuehrung des verfahrens
DE3715516A1 (de) * 1987-05-09 1988-11-17 Inter Power Technologie Wirbelschichtfeuerung
JPH03213902A (ja) * 1990-01-19 1991-09-19 Nkk Corp 循環流動層燃焼装置
FI88200C (fi) 1990-01-29 1993-04-13 Tampella Oy Ab Foerbraenningsanlaeggning
US5253741A (en) 1991-11-15 1993-10-19 Foster Wheeler Energy Corporation Fluidized bed steam reactor including two horizontal cyclone separators and an integral recycle heat exchanger
FI101156B (fi) * 1996-08-30 1998-04-30 Fortum Oil Oy Kiertomassareaktoriin perustuva menetelmä ja laite hiilivetyjen konver toimiseksi

Also Published As

Publication number Publication date
NO20020111L (no) 2002-03-14
CA2379164A1 (en) 2001-01-25
SE522657C2 (sv) 2004-02-24
AU6329800A (en) 2001-02-05
PL352496A1 (en) 2003-08-25
CZ2002101A3 (cs) 2002-10-16
EP1196719A1 (en) 2002-04-17
SE9902711L (sv) 2001-01-16
SE9902711D0 (sv) 1999-07-15
US6743280B1 (en) 2004-06-01
DE60020709D1 (de) 2005-07-14
ATE297529T1 (de) 2005-06-15
EP1196719B1 (en) 2005-06-08
AU767945B2 (en) 2003-11-27
WO2001006178A1 (en) 2001-01-25

Similar Documents

Publication Publication Date Title
ES8405637A1 (es) Procedimiento para la separacion de sustancias perjudiciales a partir de gases de escape.
TW367267B (en) The processing of exhaust gases by a chlorine bypass system and apparatus thereof
US3780497A (en) Adsorption of fluorine and fluorine compounds on alumina
FI20000262A0 (fi) Menetelmä ja laitteisto kiintoaineen erottamiseksi kaasuista
DE60041426D1 (de) Zentrifugale Trennvorrichtung und Verfahren zur Trennung von Flüssigkeitsbestandteilen
CA2059208A1 (en) Continuous discharge centrifuge
SE8502653D0 (sv) Process and apparatus for separating solid particles and gaseous materials
FI974263A0 (fi) Foerfarande och anlaeggning foer separering av fasta aemnen fraon gaser
DE60020709D1 (de) Teilchenabschneider
CA2183425A1 (en) Separation of a Suspension Into Its Component Parts
DE3574394D1 (en) Apparatus for the separation of solid particulates from a gaseous effluent
AU3034597A (en) Method of and apparatus for decreasing attack of detrimental components of solid particle suspensions on heat transfer surfaces
ATE58220T1 (de) Reaktor mit zirkulierendem wirbelbett, verfahren zum trennen von feststoffen aus rauchgas.
GB2183503B (en) Separator for separating entrained particulate solids from a gas flow
ATE492326T1 (de) Verfahren zur trennung von feststoffen von einem mit feststoffen beladenen gasstrom
RU2005122017A (ru) Кольцевой воздушный нож и способ снижения нарастания твердого материала
US3263808A (en) Method for the separation of particles of different sizes and densities
GB1474215A (en) Process for removing hydrogen fluoride from gases containing it
CA2230953A1 (en) Advanced particulate media for precise separation of particles suspended in fluids
ATE153004T1 (de) Direktgewinnung von kristallinen fullerenen aus einem fulleredampf-russ-gemisch
JPS61271045A (ja) サイクロン分離装置
ATE21920T1 (de) Verfahren zur herstellung von russpartikeln und russ-abscheidungsvorrichtung.
FI880650A (fi) Reaktor.
JPS6049947U (ja) サイクロン分離器
TH34180A (th) อุปกรณ์ในการแยกสำหรับทำให้อนุภาคของแข็งแยกจากแกสที่ไหลของชั้นที่ทำให้เลื่อนไหล

Legal Events

Date Code Title Description
FC2A Withdrawal, rejection or dismissal of laid open patent application