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Equilibrium Stage Concept
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=QUIBLIBRIUM STAGE CONCEPT STAGE unit/equipment brought into and are other During the OF The the phases the EQUILIBRIUM STAGE ACTUAL STAGE then contact in w/c two dissimilar phases intimate comact with each various mixture redistributes resultant phase mec navlically separated. a time equi librium At equilibrium there is STAGE EFFICIENCY In an equilibrium stage the two phases are well mixed For sufficient to allow between thermodynamic the establishment OF Phaces leaving the stage. no Further net exchange OF phases as long as operating conditions composition OF reniain constant the All equilibrium stage gives change possible For a given conditions. It is also referred. the oretical stage. approaches equilibrium. as an diffusing Components themselves bet ween 2₂ In actual industrial equipment it practical to time allow SUFFiCient to attain equilibrium. 20 There Fore e qui librium " accomplished Instead, an actual stage wnich change at equilibri um is Thanl 2 ratic OF composition change that in all Over all stage Efficiency: no = greatest composition operating set equilibrium stage. no. Of ideal trays Trays no. of actual OF ideal stage stage is not usually an with thorough mixing not has achieved or normally less composition. actual stage Q GAS ABSORPTION when equilibrium is. will be transferred no more transfer. there is For mass Weak Liquor SOLID LIQUID -inert liquid solute (0) STRIPPING OR DESORPTION 25 20 Rich gas inert gas. solute Extract La xai 1 LIQUID Solid Feed LIQUID EXTRACTION (a) single-stage mixer settler (b) Multi Stage mixer settler Mixer settlers phases are For liqui -liquid thoroughly mixed Flows imo the setting tank allowed TO separate under @ L (more dense) @ V- phase ( less dense) V Va opposite of gas absorption Output: va (Higher solute) LD ( Lower solute 1 reached no more solute from gas to liquid since concentration driving Force EXTRACTION Dilute gas. /Exit gas (less colute) Contact: Surface XD Y N-1 Strong. Liquor (more. salute.) arrangement extraction the by where Over all phase the UnderFlow Phase I V the influence OF N L The impeller. two entering me two phases are gravity mixture Solvent Raffinat ADSORPTION AdsorpHop Fixed Bed 180° Inert ceramic Balls Adsorbent. .Inert · Ceramic Balls. Support grid.
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This tackles the equilibrium stage, actual stage and stage efficiency. This also includes a short description about gas absorption, stripping or desorption, liquid-liquid extraction ad solid-liquid extraction.
This tackles the equilibrium stage, actual stage and stage efficiency. This also includes a short description about gas absorption, stripping or desorption, liquid-liquid extraction ad solid-liquid extraction.
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=QUIBLIBRIUM STAGE CONCEPT STAGE unit/equipment brought into and are other During the OF The the phases the EQUILIBRIUM STAGE ACTUAL STAGE then contact in w/c two dissimilar phases intimate comact with each various mixture redistributes resultant phase mec navlically separated. a time equi librium At equilibrium there is STAGE EFFICIENCY In an equilibrium stage the two phases are well mixed For sufficient to allow between thermodynamic the establishment OF Phaces leaving the stage. no Further net exchange OF phases as long as operating conditions composition OF reniain constant the All equilibrium stage gives change possible For a given conditions. It is also referred. the oretical stage. approaches equilibrium. as an diffusing Components themselves bet ween 2₂ In actual industrial equipment it practical to time allow SUFFiCient to attain equilibrium. 20 There Fore e qui librium " accomplished Instead, an actual stage wnich change at equilibri um is Thanl 2 ratic OF composition change that in all Over all stage Efficiency: no = greatest composition operating set equilibrium stage. no. Of ideal trays Trays no. of actual OF ideal stage stage is not usually an with thorough mixing not has achieved or normally less composition. actual stage Q GAS ABSORPTION when equilibrium is. will be transferred no more transfer. there is For mass Weak Liquor SOLID LIQUID -inert liquid solute (0) STRIPPING OR DESORPTION 25 20 Rich gas inert gas. solute Extract La xai 1 LIQUID Solid Feed LIQUID EXTRACTION (a) single-stage mixer settler (b) Multi Stage mixer settler Mixer settlers phases are For liqui -liquid thoroughly mixed Flows imo the setting tank allowed TO separate under @ L (more dense) @ V- phase ( less dense) V Va opposite of gas absorption Output: va (Higher solute) LD ( Lower solute 1 reached no more solute from gas to liquid since concentration driving Force EXTRACTION Dilute gas. /Exit gas (less colute) Contact: Surface XD Y N-1 Strong. Liquor (more. salute.) arrangement extraction the by where Over all phase the UnderFlow Phase I V the influence OF N L The impeller. two entering me two phases are gravity mixture Solvent Raffinat ADSORPTION AdsorpHop Fixed Bed 180° Inert ceramic Balls Adsorbent. .Inert · Ceramic Balls. Support grid.
=QUIBLIBRIUM STAGE CONCEPT STAGE unit/equipment brought into and are other During the OF The the phases the EQUILIBRIUM STAGE ACTUAL STAGE then contact in w/c two dissimilar phases intimate comact with each various mixture redistributes resultant phase mec navlically separated. a time equi librium At equilibrium there is STAGE EFFICIENCY In an equilibrium stage the two phases are well mixed For sufficient to allow between thermodynamic the establishment OF Phaces leaving the stage. no Further net exchange OF phases as long as operating conditions composition OF reniain constant the All equilibrium stage gives change possible For a given conditions. It is also referred. the oretical stage. approaches equilibrium. as an diffusing Components themselves bet ween 2₂ In actual industrial equipment it practical to time allow SUFFiCient to attain equilibrium. 20 There Fore e qui librium " accomplished Instead, an actual stage wnich change at equilibri um is Thanl 2 ratic OF composition change that in all Over all stage Efficiency: no = greatest composition operating set equilibrium stage. no. Of ideal trays Trays no. of actual OF ideal stage stage is not usually an with thorough mixing not has achieved or normally less composition. actual stage Q GAS ABSORPTION when equilibrium is. will be transferred no more transfer. there is For mass Weak Liquor SOLID LIQUID -inert liquid solute (0) STRIPPING OR DESORPTION 25 20 Rich gas inert gas. solute Extract La xai 1 LIQUID Solid Feed LIQUID EXTRACTION (a) single-stage mixer settler (b) Multi Stage mixer settler Mixer settlers phases are For liqui -liquid thoroughly mixed Flows imo the setting tank allowed TO separate under @ L (more dense) @ V- phase ( less dense) V Va opposite of gas absorption Output: va (Higher solute) LD ( Lower solute 1 reached no more solute from gas to liquid since concentration driving Force EXTRACTION Dilute gas. /Exit gas (less colute) Contact: Surface XD Y N-1 Strong. Liquor (more. salute.) arrangement extraction the by where Over all phase the UnderFlow Phase I V the influence OF N L The impeller. two entering me two phases are gravity mixture Solvent Raffinat ADSORPTION AdsorpHop Fixed Bed 180° Inert ceramic Balls Adsorbent. .Inert · Ceramic Balls. Support grid.
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