WO2022223868A1 - Reactor arrangement and use thereof - Google Patents
Reactor arrangement and use thereof Download PDFInfo
- Publication number
- WO2022223868A1 WO2022223868A1 PCT/FI2021/050287 FI2021050287W WO2022223868A1 WO 2022223868 A1 WO2022223868 A1 WO 2022223868A1 FI 2021050287 W FI2021050287 W FI 2021050287W WO 2022223868 A1 WO2022223868 A1 WO 2022223868A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- draft tube
- arrangement
- openings
- impeller
- opening
- Prior art date
Links
- 239000002002 slurry Substances 0.000 claims description 29
- 230000000903 blocking effect Effects 0.000 claims description 16
- 238000002386 leaching Methods 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 4
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 4
- 238000002156 mixing Methods 0.000 claims description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 2
- 229910017052 cobalt Inorganic materials 0.000 claims description 2
- 239000010941 cobalt Substances 0.000 claims description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- 229910052725 zinc Inorganic materials 0.000 claims description 2
- 239000011701 zinc Substances 0.000 claims description 2
- 230000008901 benefit Effects 0.000 description 28
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 10
- 239000007789 gas Substances 0.000 description 10
- 239000001301 oxygen Substances 0.000 description 10
- 229910052760 oxygen Inorganic materials 0.000 description 10
- 238000009931 pascalization Methods 0.000 description 4
- 238000005086 pumping Methods 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 230000003455 independent Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000002706 hydrostatic effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 235000015250 liver sausages Nutrition 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000136 polysorbate Polymers 0.000 description 1
- 235000019832 sodium triphosphate Nutrition 0.000 description 1
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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
-
- 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
- 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
- B01J8/222—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 in the presence of a rotating device only
-
- 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
Definitions
- the invention relates to a reactor arrangement.
- the invention further relates to uses of the reactor ar rangement.
- the participatory oxygen needed in the leaching process is introduced in the form of oxygen or gas containing oxygen and dissolved into the solid-containing slurry, so that the oxygen can partici pate in the leaching reactions of the solid matter.
- a high reactor provided with a draft tube is used for the disso lution of the oxygen, whereupon a high hydrostatic pres sure, such as 1.5-3.0 atm i.e. 0.15-0.30 MPa, is formed at the bottom of the reactor. Said high hydrostatic pressure promotes the dissolving of the oxygen in the slurry.
- a reac tor arrangement comprising a reactor tank, a draft tube arranged in the reactor tank, and an impeller arranged in the immediate vicinity of a lower end of the draft tube, wherein, the wall of the draft tube comprises openings through said wall, and wherein the total surface area of the openings as a percentage of the total outside surface area of the draft tube is 4 % at most.
- the total surface area of the openings as a percentage of the total outside surface area of the draft tube is in range of 0.5 % - 4 %. In one embodiment, the total surface area of the openings is in range of 0.5 % - 2 %.
- At least one of the openings is round.
- the width of the opening as a percent age of the outer diameter of the draft tube is in range of 5 % - 30 %, preferably 10 % - 20%.
- An advantage is that a proper flow in the draft tube may be achieved without jeopardizing mechanical strength thereof.
- the openings are arranged in opening groups comprising at least two openings and arranged suc cessively in longitudinal direction of the draft tube, and wherein in longitudinal direction of the draft tube, a distance between adjacent opening groups is larger than between the openings arranged in a same opening group.
- An advantage is that flow in the draft tube may be en hanced on those sections of the draft tube comprising said opening groups.
- the openings are evenly spaced between an opening closest to an upper end of the draft tube and an opening closest to a lower end of the draft tube.
- An advantage is that a steady flow in the draft tube inde pendent from the level of free surface may be achieved.
- the openings are of a quantity and po sition such that a fluid is capable to flow through the openings in the draft tube along substantially the entire length of the draft tube between the opening closest to a upper end of the draft tube and the opening closest to a lower end of the draft tube.
- An advantage is that the flowing capacity of the openings is concentrated to the upper sections of the draft tube where hydrostatic pressure is low, and thus a satisfactory flow in those sections in the draft tube may be ensured.
- the total area of the openings arranged in the upper half of said lengthwise section is at least 60 %.
- an advantage is that the satisfactory flow in the upper sections of the draft tube may be ensured even more.
- an upper conical extension for slurry inflow at the upper end of the draft tube there is arranged an upper conical extension for slurry inflow, the diameter of which upper conical extension ta pers towards the draft tube.
- the slurry inflow may be intensified.
- the first clearance is in range of 0.5 x D - l x D.
- a lower conical extension for accommodating an impeller, the diameter of which lower conical extension tapers towards the draft tube.
- the diameter of the impeller may be larger than the draft tube, and thus a more effective pumping may be achieved.
- the inner surface of the draft tube is provided with one or more blocking elements, such as baf fles, that is/are arranged to extend in the direction of the longitudinal direction.
- blocking elements such as baf fles
- the draft tube is arranged concentri cally with the reactor tank.
- an advantage is that an optimized room between the impel ler and the bottom of the reactor tank for creating an op timized slurry flow that enhances dissolving gas into the slurry may be achieved.
- the distance between the median level of the impeller and the lower end of the draft tube is 0.5 X D at most. In one embodiment, the distance between the median level of the impeller and the lower end of the draft tube is 0.25 X D at most.
- An advantage is that dissolving gas into the slurry may be enhanced.
- the impeller is arranged partly inside of the draft tube.
- the impeller is arranged completely outside of the draft tube.
- An advantage is that dissolving gas into the slurry may be enhanced.
- the arrangement comprises only one im peller.
- An advantage is that a high local mixing power intensity is obtained at the bottom of the reactor where gas feed is arranged, and thus gas to liquid mass transfer may be en hanced.
- the length of the draft tube may be optimized without jeopardizing the normal operation of the arrangement.
- the inner wall of the reactor tank is cylindrical having an inner diameter, and the ratio of said inner diameter to the outer diameter of the draft tube, that is R/D, is selected in range of 2 - 4.
- An advantage is that the flowing capacity of the draft tube may be optimized in relation to the volume of the re actor tank.
- an inner height of the reactor tank is at least 10 m.
- An advantage is that high hydrostatic pressure that pro- motes the dissolving of the oxygen in the slurry may be achieved.
- At least one blocking element such as a baffle, is arranged to an inner wall of the reactor tank.
- the impeller is arranged for creating a downward directed suck in the draft tube.
- the impeller is arranged at least part ly outside of the draft tube.
- An advantage is that the flow pattern in the reactor tank and outside the draft tube may be effectively influenced by the impeller.
- the impeller is arranged for creating a radially directed flow in the reactor tank.
- An advantage is that an effective dispersion of gas in the slurry may be achieved.
- An advantage is that impairing of the pumping efficiency of the impeller caused by the openings may be alleviated.
- Figure 1 is a schematic side view of a reactor arrangement in partial cross-section
- Figure 2 is a schematic side view of a draft tube
- FIG. 3 is a schematic side view of another draft tube
- Figure 4 illustrates some embodiments of openings
- Figure 5 is a schematic view of a detail of a draft tube.
- Figure 1 is a schematic side view of a reactor arrangement in partial cross-section.
- the reactor arrangement 100 com prises a reactor tank 10, a draft tube 1 arranged in the reactor tank 10, and an impeller 8 that is arranged in the immediate vicinity of a lower end 6 of the draft tube 1.
- said immediate vicinity of the im peller may guarantee a downward directed suck of slurry in the draft tube.
- the reactor arrangement can be used for mixing gas, such as oxygen or oxygen containing gas mixture, in slurry e.g. for leaching sulfidic material containing iron, nickel, cobalt, zinc and/or copper.
- gas such as oxygen or oxygen containing gas mixture
- the wall 2 of the tube has typically a circular cross- section.
- the wall 2 comprises plurality of openings 3 that extends through said wall, i.e. are through-holes.
- the to tal surface area of the openings 3 as a percentage of the total outside surface area of the draft tube 1 is 4 % at most. In one embodiment, said percentage is in range of 0.5 % - 4 %. In one embodiment, said percentage is in range of 0.5 % - 2 %. Said total area of the openings en sures a satisfactory inflow in the draft tube 1 when the slurry falls under the upper end 4 of the draft tube, but, on the other hand, prevents an excessive outflow out from the draft tube 1 under normal working conditions when the slurry inflow takes place through the upper end 4.
- the mass flow rate through the open ings 3 is not more than 30 % of the pumping mass flow rate of the impeller 8 during a normal operation of the ar rangement 100 when the slurry level is above the upper end 4 of the draft tube 1. In one embodiment, said percentage is not more than 10 %. In one embodiment, such as shown in Figure 1, all the openings 3 has a round shape. In other embodiments, not all but at least one of the openings is round. In one em bodiment, at least half of the openings 3 have a round shape.
- the inner wall of the reactor tank 10 is cylindrical having an inner diameter R.
- the reactor tank 10 may have another shape, too.
- the reactor tank 10 has a semi-ellipsoidal shape at its lower end.
- the lower end may also be shaped to e.g. a flat or a coni cal shape.
- the draft tube 1 is arranged concentri cally with the reactor tank 10. However, this is not al ways necessary.
- the reactor tank 10 is cylindrical and the ratio of its inner diameter R to the outer diameter D of the draft tube, that is R/D, is selected in range of 2 - 4. In one embodiment, said ratio is in range of 2.5 -
- an inner height of the reactor tank 10 is at least 10 m. This order of height makes it possible to reach high hydrostatic pressure in lower parts of the reactor tank and quicken dissolving of the oxygen in the slurry.
- the draft tube 1 is attached to the re actor tank 10 by at least one tube support 13.
- the tube support may comprise e.g. a bar-like or a plate-like structure.
- the median level ML is defined by the upmost and lowermost edges of the blades of the impeller in the longitudinal direction of the draft tube L.
- the im peller 8 and the draft tube 1 are positioned in the reac tor tank 10 so that the bottom clearance BC is in range of 0.8D - 1.5D, wherein the D is the outer diameter of the draft tube.
- the impeller 8 is positioned such that when measuring in the longitudinal direction of the draft tube L, there is a distance between the median level ML of the impeller 8 and the lower end 6 of the draft tube that is 0.5 X D at most. In one embodiment, said distance is 0.25 X D at most.
- the median level ML is defined by the upmost and lowermost edges of the blades of the impeller in the longitudinal direction of the draft tube L.
- the impeller 8 or its blades situate(s) completely outside of the draft tube 1.
- a top clearance TC between an upper end 4 of the draft tube and an overflow 14, such as a launder, a chute, a channel or a duct.
- the overflow 14 may define a free surface FS of slurry during normal oper ation of the arrangement 100.
- the top clearance TC being 1.0D at most, wherein the D is the out er diameter of the draft tube.
- there is at least one blocking element 9 is arranged to an inner wall of the reactor tank 10.
- the blocking element 9 may be or comprise a baffle, for in stance.
- the blocking element 9 may be arranged to extend in the direction of the longitudinal direction L.
- the blocking element 9 may be arranged parallel to L or to a position that deviates from the longitudinal direction L.
- an inner surface of the wall 2 of the draft tube is provided with one or more blocking elements 9.
- Said blocking element 9 may be or comprise a baffle that is arranged to extend in the direction of the longi tudinal direction L.
- the blocking element 9 may be ar ranged parallel to L or to a position that deviates from the longitudinal direction L.
- the arrange ment comprises only one impeller 8.
- the impeller 8 is arranged to create a downward directed suck in the draft tube 1, i.e. moving slurry inside the draft tube 1 towards the lower end 6.
- This kind of suck may be provided e.g. with suitably shaped curved impeller blades (not shown) creating axially downwards directed flow.
- the impeller 8 is arranged partly outside and partly inside of the draft tube 1.
- the impeller 8 is ar ranged to create at least partly radially (i.e. horizon tally) directed flow in the reactor tank 10.
- the radially directed flow may be created e.g. by straight blades or turbine blades (not shown) of the impeller.
- the radially directed flow disperses effectively gas fed underneath the impeller in the slurry.
- the impeller 8 comprises a first set of blades arranged in its upper part for creating axially downwards directed flow, whereas in a lower part of the impeller there is a second set of blades for creating at least partly radially directed flow.
- the impeller 8 is arranged completely outside of the draft tube 1.
- Figure 2 is a schematic side view of a draft tube.
- the openings 3 are arranged in opening groups 11.
- the opening group 11 may include two or more openings.
- the opening groups 11 are arranged successively in longitudinal direction L of the draft tube 1 so that a distance between adjacent opening groups 11 is larger than between the openings arranged in a same opening group 11.
- the number of opening groups 11 is 4 - 10 groups.
- the number of the openings 3 in one opening group 11 is selected in range of 2 - 6. It is to be noted that the number of the openings may be equal in all the opening groups 11; however, this is not necessary.
- the shape, size, placing and total area of the openings may be identical in every opening groups 11, or, alternatively, there may be variations in said variables.
- the openings 3 are evenly spaced be tween an opening closest to an upper end 4 of the draft tube 1 and an opening closest to a lower end 6 of the draft tube 1.
- the openings 3 are of a quantity and position such that slurry or liq- uid is capable to flow through said openings in the draft tube 1 along substantially the entire length of a length wise section 12 that situates between the opening closest to a upper end 4 of the draft tube and the opening closest to a lower end 6 of the draft tube.
- the lower edge of an opening positioned higher may situate at the same height position H or lower than an upper edge of another opening positioned lower.
- said lower and upper edges are positioned on the same height position H.
- the upper end 4 of the draft tube 1 is provided with an upper coni cal extension 5.
- the diameter of the upper conical exten sion 5 tapers towards the draft tube 1.
- the upper conical extension 5 may promote slurry inflow in the draft tube 1.
- first clearance Cl there is a first clearance Cl in the draft tube between the opening 3 closest to the upper end 4 and said upper end 4.
- the first clearance Cl is devoid of openings.
- the first clearance Cl is not more than the draft tube diameter D.
- the first clearance Cl is in range of 0.5 x D - l x D.
- a lower conical extension 7 tapering upwards is provided at the lower end 6 of the draft tube.
- the impeller 8 is arranged partly in side the lower conical extension 7.
- the impeller 8 is arranged below and close proximity of the lower conical extension 7.
- Figure 3 is a schematic side view of another draft tube.
- the openings 3 are arranged in the lengthwise section 12 in the draft tube so that the total area of the openings 3 in an upper half 12a of said lengthwise section 12, i.e. the half-length of the length wise section 12 closest to the upper end 4, is at least 50 % of total area of all the openings 3 arranged in the lengthwise section 12. In other words, majority of the to tal area of the openings is situated in the upper half 12a. In one embodiment, at least 60 % of said total area of the openings 3 is arranged in the upper half 12a.
- Figure 4 is illustrating some embodiments of the openings. As shown in Figures 1 - 3, the opening 3 may have a round shape.
- At least one of the openings 3 is poly gon, such as triangular, quadrangular, etc.
- At least one of the openings 3 has an oblong form, such as oval, oviform or rectangle.
- the longitudinal direction of the oblong shaped opening is arranged at least essentially parallel with the longitudinal direction L of the draft tube.
- said longitudinal direction of the oblong shaped opening is arranged at least essentially to a per pendicular direction with the longitudinal direction L.
- said longitudinal direction is arranged at an angle between the longitudinal direction and the per pendicular direction.
- the width w, i.e. dimension perpendicu lar to the longitudinal direction L, of the opening 3 de fined as a percentage of the outer diameter D of the draft tube is in range of 5 % - 30 %. In one embodiment, said percentage is 10 % - 20%. In one embodiment, the width w is selected in range of 5 cm - 100 cm. In one embodiment, the width w is selected in range of 10 cm - 60 cm. In one embodiment, the width w is selected in range of 15 cm - 20 cm.
- the height of the opening i.e. its dimension perpendicular to the width w, is selected in range of 5 cm - 75 cm. In one embodiment, the height of the opening is selected in range of 10 cm - 60 cm. In one embodiment, the height of the opening is selected in range of 15 cm - 20 cm.
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP21937770.2A EP4326427A1 (en) | 2021-04-19 | 2021-04-19 | Reactor arrangement and use thereof |
PCT/FI2021/050287 WO2022223868A1 (en) | 2021-04-19 | 2021-04-19 | Reactor arrangement and use thereof |
CN202220908965.0U CN218222402U (en) | 2021-04-19 | 2022-04-19 | Reactor device |
CN202210411278.2A CN115212828A (en) | 2021-04-19 | 2022-04-19 | Reactor device and use thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/FI2021/050287 WO2022223868A1 (en) | 2021-04-19 | 2021-04-19 | Reactor arrangement and use thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2022223868A1 true WO2022223868A1 (en) | 2022-10-27 |
Family
ID=83605933
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FI2021/050287 WO2022223868A1 (en) | 2021-04-19 | 2021-04-19 | Reactor arrangement and use thereof |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP4326427A1 (en) |
CN (2) | CN218222402U (en) |
WO (1) | WO2022223868A1 (en) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4378165A (en) * | 1980-12-30 | 1983-03-29 | General Signal Corporation | Draft tube apparatus |
US20040240315A1 (en) * | 2003-06-02 | 2004-12-02 | Balan Prakash G. | Slotted draft tube mixing systems |
WO2016023812A1 (en) * | 2014-08-14 | 2016-02-18 | Solvay Sa | Process, assembly and plant using hydrogen peroxide |
CN208177017U (en) * | 2017-12-21 | 2018-12-04 | 昆明满天红生物科技有限公司 | A kind of biology extraction element |
-
2021
- 2021-04-19 EP EP21937770.2A patent/EP4326427A1/en active Pending
- 2021-04-19 WO PCT/FI2021/050287 patent/WO2022223868A1/en active Application Filing
-
2022
- 2022-04-19 CN CN202220908965.0U patent/CN218222402U/en active Active
- 2022-04-19 CN CN202210411278.2A patent/CN115212828A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4378165A (en) * | 1980-12-30 | 1983-03-29 | General Signal Corporation | Draft tube apparatus |
US20040240315A1 (en) * | 2003-06-02 | 2004-12-02 | Balan Prakash G. | Slotted draft tube mixing systems |
WO2016023812A1 (en) * | 2014-08-14 | 2016-02-18 | Solvay Sa | Process, assembly and plant using hydrogen peroxide |
CN208177017U (en) * | 2017-12-21 | 2018-12-04 | 昆明满天红生物科技有限公司 | A kind of biology extraction element |
Non-Patent Citations (1)
Title |
---|
HONKALA ELINA: "VALIDATION AND DEVELOPMENT OF A NOVEL DRAFT TUBE REACTOR", MASTER’S THESIS, 1 May 2014 (2014-05-01), pages iii-vi, 1-83, 8-1 - 8-4, XP093000738, Retrieved from the Internet <URL:http://jultika.oulu.fi/files/nbnfioulu-201406191772.pdf> [retrieved on 20221122] * |
Also Published As
Publication number | Publication date |
---|---|
EP4326427A1 (en) | 2024-02-28 |
CN115212828A (en) | 2022-10-21 |
CN218222402U (en) | 2023-01-06 |
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