FI126361B - Reaktori nesteiden, kaasujen ja kiinteän aineen sekoittamiseksi - Google Patents

Reaktori nesteiden, kaasujen ja kiinteän aineen sekoittamiseksi Download PDF

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Publication number
FI126361B
FI126361B FI20145632A FI20145632A FI126361B FI 126361 B FI126361 B FI 126361B FI 20145632 A FI20145632 A FI 20145632A FI 20145632 A FI20145632 A FI 20145632A FI 126361 B FI126361 B FI 126361B
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reactor
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diameter
impeller
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FI20145632A
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FI20145632A (fi
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Jiliang Xia
Marko Latva-Kokko
Teemu Ritasalo
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Outotec Finland Oy
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Priority to FI20145632A priority Critical patent/FI126361B/fi
Application filed by Outotec Finland Oy filed Critical Outotec Finland Oy
Priority to CN201580037368.8A priority patent/CN106536030B/zh
Priority to PCT/FI2015/050475 priority patent/WO2016001486A1/en
Priority to EP15747498.2A priority patent/EP3160625B1/en
Priority to EA201692413A priority patent/EA031657B1/ru
Priority to NO15747498A priority patent/NO3160625T3/no
Priority to PL15747498T priority patent/PL3160625T3/pl
Priority to CA2953278A priority patent/CA2953278A1/en
Priority to AU2015282628A priority patent/AU2015282628B2/en
Priority to ES15747498.2T priority patent/ES2654180T3/es
Priority to MX2016016949A priority patent/MX2016016949A/es
Publication of FI20145632A publication Critical patent/FI20145632A/fi
Application granted granted Critical
Publication of FI126361B publication Critical patent/FI126361B/fi
Priority to CL2016003339A priority patent/CL2016003339A1/es
Priority to ZA2017/00169A priority patent/ZA201700169B/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2334—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer
    • B01F23/23341—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements provided with stationary guiding means surrounding at least partially the stirrer with tubes surrounding the stirrer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/86—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle
    • B01F27/861—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis co-operating with deflectors or baffles fixed to the receptacle the baffles being of cylindrical shape, e.g. a mixing chamber surrounding the stirrer, the baffle being displaced axially to form an interior mixing chamber
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/233—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements
    • B01F23/2336—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer
    • B01F23/23362—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using driven stirrers with completely immersed stirring elements characterised by the location of the place of introduction of the gas relative to the stirrer the gas being introduced under the stirrer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/30—Mixing gases with solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/30—Mixing gases with solids
    • B01F23/36—Mixing gases with solids by mixing in fluidised bed state
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/50—Mixing liquids with solids
    • B01F23/53—Mixing liquids with solids using driven stirrers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 
    • 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
    • B01J8/1872—Details of the fluidised bed reactor
    • 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
    • B01J8/20—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium
    • B01J8/22—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid
    • B01J8/224—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement
    • B01J8/226—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with liquid as a fluidising medium gas being introduced into the liquid the particles being subject to a circulatory movement internally, i.e. the particles rotate within the vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0409—Relationships between different variables defining features or parameters of the apparatus or process
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0413—Numerical information
    • B01F2215/0418—Geometrical information
    • B01F2215/0422—Numerical values of angles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F2215/00—Auxiliary or complementary information in relation with mixing
    • B01F2215/04—Technical information in relation with mixing
    • B01F2215/0413—Numerical information
    • B01F2215/0418—Geometrical information
    • B01F2215/0431—Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/113—Propeller-shaped stirrers for producing an axial flow, e.g. shaped like a ship or aircraft propeller
    • B01F27/1134—Propeller-shaped stirrers for producing an axial flow, e.g. shaped like a ship or aircraft propeller the impeller being of hydrofoil type
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00823—Mixing elements
    • B01J2208/00831—Stationary elements
    • B01J2208/0084—Stationary elements inside the bed, e.g. baffles
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00823—Mixing elements
    • B01J2208/00858—Moving elements
    • B01J2208/00867—Moving elements inside the bed, e.g. rotary mixer
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00893—Feeding means for the reactants
    • B01J2208/00902—Nozzle-type feeding elements
    • 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
    • B01J2208/00796—Details of the reactor or of the particulate material
    • B01J2208/00938—Flow distribution elements
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Aviation & Aerospace Engineering (AREA)
  • Mixers Of The Rotary Stirring Type (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Claims (7)

1. Reaktori nesteen, kaasun ja kiinteän aineen sekoittamiseksi, joka reaktori (10) käsittää: pystysuuntaan ulottuvan sylinterimäisen reaktoritankin (11), jossa on yläpää (12) ja suljettu pohja (13), jolla reaktoritankilla (11) edelleen on halkaisija (Dl), ja korkeus (Hl), joka on useita kertoja suurempi kuin halkaisija (Dl), imuputken (100), joka ulottuu pystysuuntaan ja samankeskisesti reaktori-tankin (11) sisällä ja joka on tuettu (14, 15) tankkiin (11), jolla imuputkella (100) on korkeus (H8), avoin yläpää (101), joka muodostaa tuloaukon, ja avoin alapää (102), joka muodostaa lähtöaukon, jolloin yläpää (101) sijaitsee korkeudella, joka muodostaa ylävälin (H3) reaktoritankissa (11) olevan materiaalin vapaan pinnankorkeuden (SL1) alapuolelle, jolloin alapää (102) sijaitsee korkeudella, joka muodostaa pohjavälin (H2) reaktoritankin (11) pohjan (13) yläpuolelle, juoksupyörän (20), joka on kytketty pystysuuntaiseen akseliin (35) ja joka sijaitsee imuputken (100) sisällä, läppäjäijestelyn (180), joka sijaitsee imuputken (100) sisällä juoksupyörän (20) alapuolella, ja kaasunsyöttölaitteen (170), joka sijaitsee imuputken (100) sisällä juoksu-pyörän (20) alapuolella, tunnettu siitä, että imuputki (100) on muodostettu jatkuvasta rakenteesta, joka käsittää neljä osuutta (110, 120, 130, 140), jotka osuudet (110, 120,130, 140) muodostuvat yläpäästä (111) alapäätä (142) kohden seuraavasti: ensimmäinen kartiomainen osuus (110), joka kapenee alapäätään (112) kohden, jolla ensimmäisellä kartiomaisella osuudella (110) on korkeus (H4) ja kar-tiokulma (ai), jolloin ensimmäisen kartiomaisen osuuden (110) yläpää muodostaa imuputken (100) yläpään (101), ensimmäinen sylinterimäinen osuus (120), jolla on halkaisija (D3) ja korkeus (H5), jonka ensimmäisen sylinterimäisen osuuden (120) yläpää yhtyy ensimmäisen kartiomaisen osuuden (110) alapäähän (112), toinen kartiomainen osuus (130), joka kapenee alapäätään (132) kohti, jolla toisella kartiomaisella osuudella (130) on korkeus (H6) ja kartiokulma (a2), jolloin toisen kartiomaisen osuuden (130) yläpää yhtyy ensimmäisen sylinterimäisen osuuden (120) alapäähän (122), ja toinen sylinterimäinen osuus (140), jolla on halkaisija (D2) ja korkeus (H7), jonka toisen sylinterimäisen osuuden (140) yläpää yhtyy toisen kartiomaisen osuuden (130) alapäähän (132), jonka toisen sylinterimäisen osuuden (140) alapää muodostaa imuputken (100) alapään (142), jolloin juoksupyörä (20) on aksiaalivirtausjuoksupyörä, joka sijaitsee ensimmäisen sylinterimäisen osuuden (120) alapäässä (122) ja pystysuuntainen akseli (35) ulottuu konsentrisesti ylöspäin reaktoritankin (11) yläpään (12) läpi, ja läppäjär-jestely (180), joka muodostuu pystysuuntaisesti ulottuvista läpistä (181, 182) sijaitsee toisen kartiomaisen osuuden (130) sisällä.
2. Patenttivaatimuksen 1 mukainen reaktori, tunnettu siitä, että reaktorin dimensiot ovat seuraavanlaiset: imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2) on edullisesti alueella 0,2-0,5 kertaa reaktoritankin (11) halkaisija (Dl), imuputken (100) ensimmäisen sylinterimäisen osuuden (120) halkaisija (D3) on edullisesti alueella 1,45 - 1,6 kertaa imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2), yläväli (H3) imuputken (100) yläpään (101) ja reaktoritankin (11) materiaalin vapaan pinnankorkeuden (SL1) välillä on edullisesti 0,4 - 0,6 kertaa imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2), pohjaväli (H2) imuputken (100) alapään (102) ja reaktoritankin (11) pohjan (13) välillä on edullisesti 1,0 - 1,4 kertaa imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2), imuputken (100) ensimmäisen sylinterimäisen osuuden (120) korkeus (H5) on edullisesti 0,8 - 1,1 kertaa imuputken (100) ensimmäisen sylinterimäisen osuuden (120) halkaisija (D3), imuputken (100) ensimmäisen kartiomaisen osuuden (110) korkeus (H4) on edullisesti 0,2 - 0,35 kertaa imuputken (100) ensimmäisen sylinterimäisen osuuden (120) halkaisija (D3), imuputken (100) ensimmäisen kartiomaisen osuuden (110) kartiokulma (ai) on edullisesti 20 - 45 astetta, edullisemmin 30 astetta, imuputken (100) toisen kartiomaisen osuuden (130) korkeus (H6) on edullisesti 0,9 - 1,1 kertaa imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2), ja edullisemmin yhtä suuri kuin imuputken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2), imuputken (100) toisen kartiomaisen osuuden (130) kartiokulma (a2) on edullisesti 8-12 astetta, edullisemmin 10 astetta, ja imuputken (100) toisen sylinterimäisen osuuden (140) korkeus (H7) laske- taan vähentämällä ylävälin (H3) korkeus, ensimmäisen kartiomaisen osuuden (110) korkeus (H4), ensimmäisen sylinterimäisen osuuden (120) korkeus (H5), toisen kartiomaisen osuuden (130) korkeus (H6), ja pohjavälin (H2) korkeus tankin (11) korkeudesta (Hl).
3. Patenttivaatimuksen 2 mukainen reaktori, tunnettu siitä, että juoksupyö-rän (20) halkaisija (D4) on edullisesti alueella 1,4 - 1,6, edullisemmin 1,5 kertaa imu-putken (100) toisen sylinterimäisen osuuden (140) halkaisija (D2).
4. Jonkin patenttivaatimusten 1-3 mukainen reaktori, tunnettu siitä, että juoksupyörällä (20) on matala leikkausjännitys ja korkea pumppauskapasiteetti.
5. Jonkin patenttivaatimusten 1-4 mukainen reaktori, tunnettu siitä, että juoksupyörän (20) siipien (40, 50, 60, 70) lukumäärä on alueella 3-5.
6. Jonkin patenttivaatimusten 1-5 mukainen reaktori, tunnettu siitä, että kaasunsyöttölaitteisto (170) sijaitsee imuputken (100) ensimmäisessä sylinterimäisessä osuudessa (120) juoksupyörän (20) ja läppäjärjestelyn (180), joka sijaitsee imuputken (100) toisessa kartiomaisessa osuudessa (130) välissä.
7. Jonkin patenttivaatimusten 1-5 mukainen reaktori, tunnettu siitä, että kaasunsyöttölaitteisto (170) sijaitsee imuputken (100) toisen kartiomaisen osuuden (130) pohjassa heti läppäjärjestelyn (180) alapuolella.
FI20145632A 2014-06-30 2014-06-30 Reaktori nesteiden, kaasujen ja kiinteän aineen sekoittamiseksi FI126361B (fi)

Priority Applications (13)

Application Number Priority Date Filing Date Title
FI20145632A FI126361B (fi) 2014-06-30 2014-06-30 Reaktori nesteiden, kaasujen ja kiinteän aineen sekoittamiseksi
AU2015282628A AU2015282628B2 (en) 2014-06-30 2015-06-29 A reactor for mixing liquid, gas and solid material
EP15747498.2A EP3160625B1 (en) 2014-06-30 2015-06-29 A reactor for mixing liquid, gas and solid material
EA201692413A EA031657B1 (ru) 2014-06-30 2015-06-29 Реактор для смешивания жидкости, газа и твердого материала
NO15747498A NO3160625T3 (fi) 2014-06-30 2015-06-29
PL15747498T PL3160625T3 (pl) 2014-06-30 2015-06-29 Reaktor do mieszania cieczy, gazu i materiału stałego
CN201580037368.8A CN106536030B (zh) 2014-06-30 2015-06-29 用于混合液体、气体和固体材料的反应器
PCT/FI2015/050475 WO2016001486A1 (en) 2014-06-30 2015-06-29 A reactor for mixing liquid, gas and solid material
ES15747498.2T ES2654180T3 (es) 2014-06-30 2015-06-29 Un reactor para mezclar material líquido, gas y sólido
MX2016016949A MX2016016949A (es) 2014-06-30 2015-06-29 Un reactor para mezclar material liquido, gas y solido.
CA2953278A CA2953278A1 (en) 2014-06-30 2015-06-29 A reactor for mixing liquid, gas and solid material
CL2016003339A CL2016003339A1 (es) 2014-06-30 2016-12-26 Reactor para mezclar material sólido, gaseoso y líquido, donde dicho reactor comprende un tanque de reactor cilíndrico que se extiende verticalmente y tiene un extremo superior y un fondo cerrado, donde se tiene un tubo de aspiración con porciones cilíndricas y cónicas
ZA2017/00169A ZA201700169B (en) 2014-06-30 2017-01-09 A reactor for mixing liquid, gas and solid material

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FI20145632A FI126361B (fi) 2014-06-30 2014-06-30 Reaktori nesteiden, kaasujen ja kiinteän aineen sekoittamiseksi

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FI126361B true FI126361B (fi) 2016-10-31

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EP (1) EP3160625B1 (fi)
CN (1) CN106536030B (fi)
AU (1) AU2015282628B2 (fi)
CA (1) CA2953278A1 (fi)
CL (1) CL2016003339A1 (fi)
EA (1) EA031657B1 (fi)
ES (1) ES2654180T3 (fi)
FI (1) FI126361B (fi)
MX (1) MX2016016949A (fi)
NO (1) NO3160625T3 (fi)
PL (1) PL3160625T3 (fi)
WO (1) WO2016001486A1 (fi)
ZA (1) ZA201700169B (fi)

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CA3088865A1 (en) * 2018-01-17 2019-07-25 Outotec (Finland) Oy Reactor for gas-liquid mass transfer
WO2024047123A1 (en) * 2022-08-30 2024-03-07 Katholieke Universiteit Leuven Swirl reactor

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* Cited by examiner, † Cited by third party
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ES2654180T3 (es) 2018-02-12
PL3160625T3 (pl) 2018-03-30
EA201692413A1 (ru) 2017-06-30
AU2015282628B2 (en) 2018-02-01
CN106536030A (zh) 2017-03-22
MX2016016949A (es) 2017-06-19
CA2953278A1 (en) 2016-01-07
WO2016001486A1 (en) 2016-01-07
ZA201700169B (en) 2018-04-25
CL2016003339A1 (es) 2017-05-26
EP3160625B1 (en) 2017-10-18
EP3160625A1 (en) 2017-05-03
CN106536030B (zh) 2019-01-01
FI20145632A (fi) 2015-12-31
NO3160625T3 (fi) 2018-03-17

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