Sequencing Separation Trains.ppt
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The document discusses separation methods for mixtures. It introduces various separation techniques like distillation, absorption, adsorption. The key factors in selecting a separation method are the feed condition (liquid, vapor, solid) and the separation factor which defines the degree of separation achievable. Distillation is commonly used for vapor-liquid separations while liquid-liquid extraction and crystallization are used for liquid separations.
Sequencing Separation Trains.ppt
- 2. Process Design/Retrofit Steps Assess Primitive Problem Development of Base-case Plant-wide Controllability Assessment Detailed Design, Equipment sizing, Cap. Cost Estimation, Profitability Analysis, Optimization Detailed Process Synthesis - Algorithmic Methods PART II
- 4. Lecture 4 – Introduction • Almost all chemical processes require the separation of chemical species (components), to: Purify a reactor feed Recover unreacted species for recycle to a reactor Separate and purify the products from a reactor • Frequently, the major investment and operating costs of a process will be associated with separation equipment • For a binary mixture, it may be possible to select a separation method that can accomplish the separation task in just one piece of equipment. • More commonly, the feed mixture involves more than two components, involving more complex separation systems.
- 5. Lecture 4 – Objectives Be familiar with the more widely used industrial separation methods and their basis for separation. Understand the concept of the separation factor and be able to select appropriate separation methods for liquid mixtures.
- 6. Example: Butenes Recovery 3.31 196.3 36.1 F n-Pentane 4.02 161.4 3.7 E cis-2-Butene 4.12 155.4 0.9 D trans-2-Butene 3.73 152.0 -0.5 C n-Butane 3.94 146.4 -6.3 B 1-Butene 4.17 97.7 -42.1 A Propane Pc, (MPa) Tc (C) b.pt.(C) Species 3.31 196.3 36.1 F n-Pentane 4.02 161.4 3.7 E cis-2-Butene 4.12 155.4 0.9 D trans-2-Butene 3.73 152.0 -0.5 C n-Butane 3.94 146.4 -6.3 B 1-Butene 4.17 97.7 -42.1 A Propane Pc, (MPa) Tc (C) b.pt.(C) Species
- 7. Example: Butenes Recovery 100-tray column C3 & 1-Butene in distillate Propane and 1-Butene recovery Pentane withdrawn as bottoms n-C4 and 2-C4=s cannot be separated by ordinary distillation (=1.03), so 96% furfural is added as an extractive agent ( 1.17). n-C4 withdrawn as distillate. 2-C4=s withdrawn as distillate. Furfural is recovered as bottoms and recycled to C-4
- 8. Separation is Energy Intensive • Unlike the spontaneous mixing of chemical species, the separation of a mixture of chemicals requires an expenditure of some form of energy • Separation of a feed mixture into streams of differing chemical composition is achieved by forcing the different species into different spatial locations, by one or a combination of four common industrial techniques: The creation by heat transfer, shaft work, or pressure reduction of a second phase that is immiscible with the feed phase (ESA – energy separating agent) Introduction into the system of a second fluid phase (MSA – mass separating agent). This must be subsequently removed. Addition of a solid phase upon which adsorption can occur Placement of a membrane barrier
- 9. Common Separation Methods difference in volatility V and L Liquid entrainer and heat transfer L and/or V Azeotropic Distillation difference in volatility V and L Liquid solvent and heat transfer L and/or V Extractive Distillation difference in volatility V Vapor stripping agent L Stripping difference in volatility L Liquid absorbent V Gas Absorption difference in volatility V or L Heat transfer or shaft work L and/or V Distillation difference in volatility V or L Pressure reduction or heat transfer L and/or V Equilibrium flash Separation principle Developed or added phase Separation agent Phase of the feed Separation Method difference in volatility V and L Liquid entrainer and heat transfer L and/or V Azeotropic Distillation difference in volatility V and L Liquid solvent and heat transfer L and/or V Extractive Distillation difference in volatility V Vapor stripping agent L Stripping difference in volatility L Liquid absorbent V Gas Absorption difference in volatility V or L Heat transfer or shaft work L and/or V Distillation difference in volatility V or L Pressure reduction or heat transfer L and/or V Equilibrium flash Separation principle Developed or added phase Separation agent Phase of the feed Separation Method
- 10. Common Separation Methods difference in permeability and/or solubility Membrane Membrane L or V Membranes difference in adsorbabililty Solid Solid adsorbent L Liquid adsorption difference in adsorbabililty Solid Solid adsorbent V Gas adsorption Difference in solubility or m.p. Solid Heat transfer L Crystalli- zation Difference in solubility Second liquid Liquid solvent L Liquid-liquid Extraction Separation principle Developed or added phase Separation agent Phase of the feed Separation Method difference in permeability and/or solubility Membrane Membrane L or V Membranes difference in adsorbabililty Solid Solid adsorbent L Liquid adsorption difference in adsorbabililty Solid Solid adsorbent V Gas adsorption Difference in solubility or m.p. Solid Heat transfer L Crystalli- zation Difference in solubility Second liquid Liquid solvent L Liquid-liquid Extraction Separation principle Developed or added phase Separation agent Phase of the feed Separation Method
- 11. Common Separation Methods Difference in volatility V Heat transfer S and L Drying Difference in solubility L Liquid solvent S Leaching Difference in solubility Supercritical fluid Supercritical solvent L or V Supercritical extraction Separation principle Developed or added phase Separation agent Phase of the feed Separation Method Difference in volatility V Heat transfer S and L Drying Difference in solubility L Liquid solvent S Leaching Difference in solubility Supercritical fluid Supercritical solvent L or V Supercritical extraction Separation principle Developed or added phase Separation agent Phase of the feed Separation Method
- 12. Separation Method Selection • The development of a separation process requires the selection of: Separation methods ESAs and/or MSAs Separation equipment Optimal arrangement or sequencing of the equipment Optimal operating temperature and pressure for the equipment • Selection of separation method depends on feed condition: • Vapor Partial condensation, distillation, absorption, adsorption, gas permeation (membranes) • Liquid Distillation, stripping, LL extraction, supercritical extraction, crystallization, adsorption, and dialysis or reverse osmosis (membranes) • Solid If wet drying, if dry leaching
- 13. Separation Method Selection • The separation factor, SF, defines the degree of separation achievable between two key components of the feed. This factor, for separation of component 1 from component 2 between phases I & II, for a single stage of contacting, is: II II I I C C C C SF 2 1 2 1 / / (8.1) C = composition variable, I, II = phases rich in components 1 and 2. • SF is generally limited by thermodynamic equilibrium. For example, in the case of distillation, using mole fractions as the composition variable and letting phase I be the vapor and phase II be the liquid, the limiting value of SF is given in terms of vapor-liquid equilibrium ratios (K-values) as: (8.2), (8.3) 1 1 1 1 1 2 2 2 2 2 for ideal L and V s , s y / x K P SF y / x K P
- 14. Separation Method Selection • For vapor-liquid separation operations that use an MSA that causes the formation of a non-ideal liquid solution (e.g. extractive distillation): (8.5) s L s L P P SF 2 2 1 1 2 , 1 • If the MSA is used to create two liquid phases, such as in liquid- liquid extraction, the SF is referred to as the relative selectivity, β , where: I I II II SF 2 1 2 1 2 , 1 / / (8.6) • In general, MSAs for extractive distillation and liquid-liquid extraction are selected according to their ease of recovery for recycle and to achieve relatively large values of SF.
- 15. Equal Cost Separators Ref: Souders (1964) Extractive distillation should NOT be used when α for ordinary distillation is greater than 2 Liquid-Liquid Extraction should NOT be used when α for ordinary distillation is greater than 3.2
- 16. Summary – Separation Trains Be familiar with the more widely used industrial separation methods and their basis for separation. Understand the concept of the separation factor and be able to select appropriate separation methods for liquid mixtures. On completion of this part, you should: