Kalkulacja/kinetika zużycia substratu w uprawach w serii i ciągłych uprawach

Uzgodnienie, że kinetyka tych of substrate consumption is essential for optimizing microbial growth in bioreactors. It involves analyzing how substrates are utilizad over time in both batch and continuous cultures. Thii knowledgge helps in controling process parameters and improwiing product yelds.

Substrate Consumption in Batch Cultures

Te substraty, które są konsumowane, są modelowane przez using kinetic equations such as Monod kinetics, which ich relate substrate concentration to microbial growth rate.

Te Monode equation is expressed as:

(S / (K) 1; PFLT: 3; PFL: 3; PFL: 1 PFS; PFL: 3; PFL: 3; PFL: 3; PFL: 4 PFM; PFS: 3; PFS: 3; PFL: 3; PFL: 3; PFS: 3; PFS: 3; PFS: 3; PFS; PFL: 3; PFS: PFS: 1; PFS: PFS: PFS: 3; PFS: PFS: 3; PFS: PFS: PFS: PFLAN: PLAN: 3; PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN: PLAN

where μis the specific growth rate, μης 1; Τη1; FLT: 0, 3; XI3; max Xi1; XI1; FLT: 1, XI3; is the maximum em specific growth rate, S is the substrate concentration, and K XI1; XI1; FLT: 2, XI3; s XI1; FLT: 3, XI3; IF: 3; ITS the this half-sation constant.

Substrate Consumption in Continuous Cultures

Nie ma żadnych stałych kultur, substratów, które mogą być nadal obecne, ani też tych, które mają stałe funkcje. Te substraty konsumpcyjne zależą od tych, które mają wpływ na mikrobial biomasa. Te procesy i ich właściwości opisują sposób użycia tych chemostatów.

Te stałe-stany substrate concentration (S) can be calculated using thee equation:

(K = 1; FLT: 1; FLT: 0 = 3; FLT: 1 = 3; FLT: 1 = 3; FL3; FLT: 1; FLT: 2 = 3; FLT: 3; FLT: 3; FL3; FL3; FL3; FL3; FL3; FL3; FL3; FL3; - D) = 1; FLT: 5 = 3; FLT: 3; FLT: 3; FL3; FL3; FL3; FL3; FL3; FL3; FLF) FLT; FLF 1; FLF 1; FL3; FL3; FL3; FLL; FLL; FLT 1; FLT: 5 = 3; FLL 3; FLS; FL3; FLS; FLS: 3; FLLS: 1; FLS: 1; FLLS: 1; FLS: 3; FLLS: 3; FLL@@

Calculating Substrate Consumption Rate

Te substraty konsumption rate (q, Q1; X1; FLT: 0, X3; X3; S, X1; X1, FLT: 1, X3;) is often expressed as:

(D * S = 1; FLT: 0 = 3; FLT: 1 = 3; FLT: 1 = 3; FLT: 1 = 3; FLT: 1; S = 1; FLT: 2 = 3; FLT = 1; FLT = 1; FLT = 1; FLT = 3 = 3; FLT = 3; FL3; FL3; FLT = 1; FLT = 4 = 3; FLT = 1; FLT = 1; FLT = 1; FLT = 3; FL3; FL3; FL3; FL3; FLS = 1; FLT = 4 = 3; FLLL3; FL3; FLS) / X = 1; FLLT = 1; FLT = 5 = 3; FLLS = 3; FLS = 3; FLS = 1; FLS = 1; FLLLT = 1 = 1 = 1; FLLS = 1 = 1 = 1 = 1; FLLL1 = 1 = 1 = 1

where D is the dilution rate, S Booking 1; Xi1; FLT: 0 XI3; in XI1; XI1; FLT: 1 XI3; XI3; is the substrate concentration in thee feed, S is the residual substrate concentration, and X is the biomass concentration.