mixing and cfd module of comsol®multiphysics 5.2 (COMSOL Inc)
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mixing and cfd module of comsol®multiphysics 5.2
Mixing And Cfd Module Of Comsol®Multiphysics 5.2, supplied by COMSOL Inc, used in various techniques. Bioz Stars score: 90/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/mixing+and+cfd+module+of+comsol%C2%AEmultiphysics+5%2E2/mixing+and+cfd+module+of+comsol+multiphysics+5+2/10__1016_slash_j__rineng__2024__102588-242-283-283
Average 90 stars, based on 1 article reviews
Mixing And Cfd Module Of Comsol®Multiphysics 5.2, supplied by COMSOL Inc, used in various techniques. Bioz Stars score: 90/100, based on 1 PubMed citations. ZERO BIAS - scores, article reviews, protocol conditions and more
https://www.bioz.com/product/mixing+and+cfd+module+of+comsol%C2%AEmultiphysics+5%2E2/mixing+and+cfd+module+of+comsol+multiphysics+5+2/10__1016_slash_j__rineng__2024__102588-242-283-283
Average 90 stars, based on 1 article reviews
mixing and cfd module of comsol®multiphysics 5.2 - by Bioz Stars,
2026-11
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Concentration Assay:Article Title: Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale Article Snippet: Symbols used A [m3/(kg.s)] pre-exponential factor a [m− 1] specific interfacial area Boz [m] baffle clearance C [m] impeller bottom clearance c(o)gum [kg/m 3] gum concentration in the oil phase c(w)gum [kg/m 3] gum concentration in the water phase cph [kg/m3] phosphate concentration Cd [− ] drag force coefficient (continued on next page) (continued ) Cμ [− ] turbulence model constant DAB [m2/s] diffusivity coefficient Ea [J/(mol.K)] activation energy Dimp [m] impeller diameter Dmd [m2/s] turbulence dispersion coefficient Dr [m] reactor diameter dd [m] drop diameter F [N/m2] total force flux g [m/s2] gravity acceleration I [− ] identity matrix Keq [− ] solubility coefficient k [m2/s2] turbulence kinetic energy kc [m/s] total mass transfer coefficient kca [1/s] Volumetric mass transfer coefficient krx [m3/(kg.s)] reaction rate constant N [1/s] impeller speed nd [1/m3] drop number density p [Pa] pressure Pk [W/m3] turbulent kinetic energy source term Red [− ] drop Reynolds number Sc [− ] Schmidt number Shd [− ] Sherwood number T [K] reacting temperature u [m/s] mixture velocity uc [m/s] continuous phase velocity ud [m/s] dispersed phase velocity udc [m/s] drop relative velocity uslip [m/s] slip velocity ε [m2/s3] turbulence dissipation rate φd [− ] dispersed-phase volume fraction μ [kg m/s] mixture viscosity μc [kg m/s] continuous phase viscosity μd [kg m/s] dispersed phase viscosity μT [kg m/s] turbulent viscosity ρ [kg/m3] mixture density ρc [kg/m 3] continuous phase density ρd [kg/m 3] dispersed phase density σk [N/m2] turbulence model constant σε [N/m2] turbulence model constant σε2 [N/m2] turbulence model constant Statement of competing interests The simulation was conducted in the Chemical Process Simulation Laboratory of the Department of Chemical Engineering, University of Indonesia using the Mixing and CFD Module of Activation Assay:Article Title: Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale Article Snippet: Symbols used A [m3/(kg.s)] pre-exponential factor a [m− 1] specific interfacial area Boz [m] baffle clearance C [m] impeller bottom clearance c(o)gum [kg/m 3] gum concentration in the oil phase c(w)gum [kg/m 3] gum concentration in the water phase cph [kg/m3] phosphate concentration Cd [− ] drag force coefficient (continued on next page) (continued ) Cμ [− ] turbulence model constant DAB [m2/s] diffusivity coefficient Ea [J/(mol.K)] activation energy Dimp [m] impeller diameter Dmd [m2/s] turbulence dispersion coefficient Dr [m] reactor diameter dd [m] drop diameter F [N/m2] total force flux g [m/s2] gravity acceleration I [− ] identity matrix Keq [− ] solubility coefficient k [m2/s2] turbulence kinetic energy kc [m/s] total mass transfer coefficient kca [1/s] Volumetric mass transfer coefficient krx [m3/(kg.s)] reaction rate constant N [1/s] impeller speed nd [1/m3] drop number density p [Pa] pressure Pk [W/m3] turbulent kinetic energy source term Red [− ] drop Reynolds number Sc [− ] Schmidt number Shd [− ] Sherwood number T [K] reacting temperature u [m/s] mixture velocity uc [m/s] continuous phase velocity ud [m/s] dispersed phase velocity udc [m/s] drop relative velocity uslip [m/s] slip velocity ε [m2/s3] turbulence dissipation rate φd [− ] dispersed-phase volume fraction μ [kg m/s] mixture viscosity μc [kg m/s] continuous phase viscosity μd [kg m/s] dispersed phase viscosity μT [kg m/s] turbulent viscosity ρ [kg/m3] mixture density ρc [kg/m 3] continuous phase density ρd [kg/m 3] dispersed phase density σk [N/m2] turbulence model constant σε [N/m2] turbulence model constant σε2 [N/m2] turbulence model constant Statement of competing interests The simulation was conducted in the Chemical Process Simulation Laboratory of the Department of Chemical Engineering, University of Indonesia using the Mixing and CFD Module of Dispersion:Article Title: Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale Article Snippet: Symbols used A [m3/(kg.s)] pre-exponential factor a [m− 1] specific interfacial area Boz [m] baffle clearance C [m] impeller bottom clearance c(o)gum [kg/m 3] gum concentration in the oil phase c(w)gum [kg/m 3] gum concentration in the water phase cph [kg/m3] phosphate concentration Cd [− ] drag force coefficient (continued on next page) (continued ) Cμ [− ] turbulence model constant DAB [m2/s] diffusivity coefficient Ea [J/(mol.K)] activation energy Dimp [m] impeller diameter Dmd [m2/s] turbulence dispersion coefficient Dr [m] reactor diameter dd [m] drop diameter F [N/m2] total force flux g [m/s2] gravity acceleration I [− ] identity matrix Keq [− ] solubility coefficient k [m2/s2] turbulence kinetic energy kc [m/s] total mass transfer coefficient kca [1/s] Volumetric mass transfer coefficient krx [m3/(kg.s)] reaction rate constant N [1/s] impeller speed nd [1/m3] drop number density p [Pa] pressure Pk [W/m3] turbulent kinetic energy source term Red [− ] drop Reynolds number Sc [− ] Schmidt number Shd [− ] Sherwood number T [K] reacting temperature u [m/s] mixture velocity uc [m/s] continuous phase velocity ud [m/s] dispersed phase velocity udc [m/s] drop relative velocity uslip [m/s] slip velocity ε [m2/s3] turbulence dissipation rate φd [− ] dispersed-phase volume fraction μ [kg m/s] mixture viscosity μc [kg m/s] continuous phase viscosity μd [kg m/s] dispersed phase viscosity μT [kg m/s] turbulent viscosity ρ [kg/m3] mixture density ρc [kg/m 3] continuous phase density ρd [kg/m 3] dispersed phase density σk [N/m2] turbulence model constant σε [N/m2] turbulence model constant σε2 [N/m2] turbulence model constant Statement of competing interests The simulation was conducted in the Chemical Process Simulation Laboratory of the Department of Chemical Engineering, University of Indonesia using the Mixing and CFD Module of Solubility:Article Title: Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale Article Snippet: Symbols used A [m3/(kg.s)] pre-exponential factor a [m− 1] specific interfacial area Boz [m] baffle clearance C [m] impeller bottom clearance c(o)gum [kg/m 3] gum concentration in the oil phase c(w)gum [kg/m 3] gum concentration in the water phase cph [kg/m3] phosphate concentration Cd [− ] drag force coefficient (continued on next page) (continued ) Cμ [− ] turbulence model constant DAB [m2/s] diffusivity coefficient Ea [J/(mol.K)] activation energy Dimp [m] impeller diameter Dmd [m2/s] turbulence dispersion coefficient Dr [m] reactor diameter dd [m] drop diameter F [N/m2] total force flux g [m/s2] gravity acceleration I [− ] identity matrix Keq [− ] solubility coefficient k [m2/s2] turbulence kinetic energy kc [m/s] total mass transfer coefficient kca [1/s] Volumetric mass transfer coefficient krx [m3/(kg.s)] reaction rate constant N [1/s] impeller speed nd [1/m3] drop number density p [Pa] pressure Pk [W/m3] turbulent kinetic energy source term Red [− ] drop Reynolds number Sc [− ] Schmidt number Shd [− ] Sherwood number T [K] reacting temperature u [m/s] mixture velocity uc [m/s] continuous phase velocity ud [m/s] dispersed phase velocity udc [m/s] drop relative velocity uslip [m/s] slip velocity ε [m2/s3] turbulence dissipation rate φd [− ] dispersed-phase volume fraction μ [kg m/s] mixture viscosity μc [kg m/s] continuous phase viscosity μd [kg m/s] dispersed phase viscosity μT [kg m/s] turbulent viscosity ρ [kg/m3] mixture density ρc [kg/m 3] continuous phase density ρd [kg/m 3] dispersed phase density σk [N/m2] turbulence model constant σε [N/m2] turbulence model constant σε2 [N/m2] turbulence model constant Statement of competing interests The simulation was conducted in the Chemical Process Simulation Laboratory of the Department of Chemical Engineering, University of Indonesia using the Mixing and CFD Module of Viscosity:Article Title: Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale Article Snippet: Symbols used A [m3/(kg.s)] pre-exponential factor a [m− 1] specific interfacial area Boz [m] baffle clearance C [m] impeller bottom clearance c(o)gum [kg/m 3] gum concentration in the oil phase c(w)gum [kg/m 3] gum concentration in the water phase cph [kg/m3] phosphate concentration Cd [− ] drag force coefficient (continued on next page) (continued ) Cμ [− ] turbulence model constant DAB [m2/s] diffusivity coefficient Ea [J/(mol.K)] activation energy Dimp [m] impeller diameter Dmd [m2/s] turbulence dispersion coefficient Dr [m] reactor diameter dd [m] drop diameter F [N/m2] total force flux g [m/s2] gravity acceleration I [− ] identity matrix Keq [− ] solubility coefficient k [m2/s2] turbulence kinetic energy kc [m/s] total mass transfer coefficient kca [1/s] Volumetric mass transfer coefficient krx [m3/(kg.s)] reaction rate constant N [1/s] impeller speed nd [1/m3] drop number density p [Pa] pressure Pk [W/m3] turbulent kinetic energy source term Red [− ] drop Reynolds number Sc [− ] Schmidt number Shd [− ] Sherwood number T [K] reacting temperature u [m/s] mixture velocity uc [m/s] continuous phase velocity ud [m/s] dispersed phase velocity udc [m/s] drop relative velocity uslip [m/s] slip velocity ε [m2/s3] turbulence dissipation rate φd [− ] dispersed-phase volume fraction μ [kg m/s] mixture viscosity μc [kg m/s] continuous phase viscosity μd [kg m/s] dispersed phase viscosity μT [kg m/s] turbulent viscosity ρ [kg/m3] mixture density ρc [kg/m 3] continuous phase density ρd [kg/m 3] dispersed phase density σk [N/m2] turbulence model constant σε [N/m2] turbulence model constant σε2 [N/m2] turbulence model constant Statement of competing interests The simulation was conducted in the Chemical Process Simulation Laboratory of the Department of Chemical Engineering, University of Indonesia using the Mixing and CFD Module of |