PL434353A1 - Method of mixing liquid with gas in a gas-tight tubular multireactor and a device for mixing liquid with gas - Google Patents
Method of mixing liquid with gas in a gas-tight tubular multireactor and a device for mixing liquid with gasInfo
- Publication number
- PL434353A1 PL434353A1 PL434353A PL43435320A PL434353A1 PL 434353 A1 PL434353 A1 PL 434353A1 PL 434353 A PL434353 A PL 434353A PL 43435320 A PL43435320 A PL 43435320A PL 434353 A1 PL434353 A1 PL 434353A1
- Authority
- PL
- Poland
- Prior art keywords
- gas
- mixing chamber
- multireactor
- tubular
- main
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title abstract 5
- 238000000034 method Methods 0.000 title abstract 2
- 239000000203 mixture Substances 0.000 abstract 1
- 239000003380 propellant Substances 0.000 abstract 1
- 239000011555 saturated liquid Substances 0.000 abstract 1
Classifications
-
- 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
- B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
- B01F23/2323—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles by circulating the flow in guiding constructions or conduits
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
- B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3123—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements
- B01F25/31233—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with two or more Venturi elements used successively
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
- B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
- B01F25/31243—Eductor or eductor-type venturi, i.e. the main flow being injected through the venturi with high speed in the form of a jet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/32—Injector mixers wherein the additional components are added in a by-pass of the main flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
- B01F25/4331—Mixers with bended, curved, coiled, wounded mixing tubes or comprising elements for bending the flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/811—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more consecutive, i.e. successive, mixing receptacles or being consecutively arranged
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
Abstract
Sposób mieszania cieczy z gazem, w gazoszczelnym multireaktorze rurowym, w którym zmieszaną ciecz z gazem, w postaci strumienia napędowego, doprowadza się do części przedniej, przy dnie lub w kierunku dna, głównej komory mieszania multireaktora rurowego, a nasyconą gazem ciecz, jako główną część strumienia napędowego, odprowadza się z części tylnej głównej komory mieszania multireaktora rurowego i doprowadza się ją do co najmniej jednej dodatkowej komory mieszania multireaktora rurowego, przy czym, dodatkowa komora mieszania lub zespół dodatkowych komór mieszania ma co najmniej dwukrotnie mniejsze pole przekroju poprzecznego od pola przekroju poprzecznego głównej komory mieszania multireaktora rurowego, charakteryzuje się tym, że mieszaninę nierozpuszczonego w cieczy gazu oraz część cieczy z głównej komory mieszania (2) zasysa się, pod wpływem energii kinetycznej głównej części strumienia napędowego (15) dopływającej do dodatkowej komory mieszania (5) dzięki połączeniu obejściowemu (6), wyprowadzonemu ze stropu (2.4) głównej komory mieszania (2) multireaktora rurowego (1) i doprowadzonemu do dodatkowej komory mieszania (5), zgodnie z równaniem Bernulliego, przy czym co najmniej jedna dodatkowa komora mieszania (5) posiada, na swym odpływie zwężającą się w stronę odpływu dyszę strumienicową (4), w której prędkość przepływu, na dopływie do niej, jest co najmniej trzykrotnie mniejsza niż wynosi prędkość na odpływie z dyszy strumienicowej (4).A method of mixing liquid with gas, in a gas-tight tubular multireactor, in which the mixed liquid with gas, in the form of a propulsion jet, is fed to the front part, at the bottom or towards the bottom, of the main mixing chamber of the tubular multireactor, and the gas-saturated liquid as the main part of the propellant stream is discharged from the rear part of the main mixing chamber of the tubular multireactor and fed to at least one additional mixing chamber of the tubular multireactor, the additional mixing chamber or a set of additional mixing chambers having a cross-sectional area at least twice smaller than the cross-sectional area the main mixing chamber of the tubular multireactor, characterized in that the mixture of the undissolved gas and part of the liquid from the main mixing chamber (2) are sucked under the influence of the kinetic energy of the main part of the propulsion stream (15) flowing into the additional mixing chamber (5) thanks to the combination bypass (6) led out from the roof (2.4) of the main mixing chamber (2) of the tubular multireactor (1) and fed to the additional mixing chamber (5), according to the Bernulli equation, at least one additional mixing chamber (5) having a narrowing outlet at its outlet downstream the jet nozzle (4), in which the flow velocity at the inlet to it is at least three times lower than the velocity at the outlet from the jet nozzle (4).
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL434353A PL243753B1 (en) | 2020-06-17 | 2020-06-17 | Method for mixing liquid with gas in a gas-tight tubular multireactor and device for mixing liquid with gas in the form of a tubular multireactor |
| PCT/IB2021/055376 WO2021255692A1 (en) | 2020-06-17 | 2021-06-17 | Method of mixing liquid with gas in a gas-tight multi-tube reactor and a device for mixing liquid with gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| PL434353A PL243753B1 (en) | 2020-06-17 | 2020-06-17 | Method for mixing liquid with gas in a gas-tight tubular multireactor and device for mixing liquid with gas in the form of a tubular multireactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| PL434353A1 true PL434353A1 (en) | 2021-12-20 |
| PL243753B1 PL243753B1 (en) | 2023-10-09 |
Family
ID=77274812
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PL434353A PL243753B1 (en) | 2020-06-17 | 2020-06-17 | Method for mixing liquid with gas in a gas-tight tubular multireactor and device for mixing liquid with gas in the form of a tubular multireactor |
Country Status (2)
| Country | Link |
|---|---|
| PL (1) | PL243753B1 (en) |
| WO (1) | WO2021255692A1 (en) |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT391849B (en) * | 1985-07-17 | 1990-12-10 | Waagner Biro Ag | METHOD FOR FUMING AND DEVICE FOR CARRYING OUT THE SAME |
| JPS6388027A (en) * | 1986-10-01 | 1988-04-19 | Mitsubishi Rayon Eng Co Ltd | Gas-liquid mixing apparatus |
| GB2366526A (en) * | 2000-09-06 | 2002-03-13 | Tsai Tsung Hsin | Pond aerator or oxygenator with entrainment of air using water pressure |
| JP6118544B2 (en) * | 2012-11-29 | 2017-04-19 | Idec株式会社 | Fine bubble generating nozzle and fine bubble generating device |
-
2020
- 2020-06-17 PL PL434353A patent/PL243753B1/en unknown
-
2021
- 2021-06-17 WO PCT/IB2021/055376 patent/WO2021255692A1/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| PL243753B1 (en) | 2023-10-09 |
| WO2021255692A1 (en) | 2021-12-23 |
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