www.modularprocess.com Telephone: (201) 267-8670 LIQUID-LIQUID EXTRACTION An Introduction 45 Eisenhower Drive, Suite 350, Paramus, NJ 07652 | Te l : ( 2 0 1 ) 2 6 7- 8 6 7 0 | Fax: (201) 368-8989 | www.modularprocess.com WHO IS ? Koch Modular Process Systems (KMPS) is a joint venture with KochGlitsch LP, one of the world's most prominent suppliers of mass transfer equipment. Koch-Glitsch's parent company is Koch Industries, one of the largest privately held corporations in the United States. For over 20 years KMPS has successfully designed and constructed mass transfer systems for the worldwide Chemical Processing Industry. Our customer’s rely upon KMPS for our quality products and technical expertise. 2 Hierarchy of Separation Technologies MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG www.modularprocess.com 3 Telephone: (201) 267-8670 Typical Applications MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG When is it prudent to use extraction? When you want to: • Remove products and pollutants from dilute aqueous streams • Wash polar compounds or acids/bases from organic streams • Separate heat sensitive products • Purify non-volatile materials • Process azeotropic and close boiling mixtures • Avoid a high cost distillation solution www.modularprocess.com 4 Telephone: (201) 267-8670 Industries Using Extraction Technology MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Chemical •Washing of acids/bases, polar compounds from organics •Recovery of valuable chemicals from aqueous solutions Biochemical Processing • Recovery of carboxylic acid from fermentation broths • Recovery of valuable “oil” from algae broths Effluent Treatment • Recovery of phenol, DMF, DMAC • Recovery of acetic acid from dilute solutions Pharmaceuticals • Recovery of active materials from fermentation broths • Purification of vitamin products Polymer Processing • Recovery of caprolactam for nylon manufacture • Separation of catalyst from reaction products www.modularprocess.com 5 Telephone: (201) 267-8670 Industries Using Extraction Technology MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Petroleum • Lube oil quality improvement • Separation of aromatics/aliphatics (BTX) Food • Decaffeination of coffee and tea • Separation of essential oils (flavors and fragrances) Metals • Copper production • Recovery of rare earth elements Inorganic Chemicals • Purification of phosphoric acid Nuclear • Purification of uranium www.modularprocess.com 6 Telephone: (201) 267-8670 Removal of Organics From Water: Distillation vs. Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG BP [°C] Water Solu. [%] Azeotrope B.P. [°C] Azeotrope Water [%] 40 2.0 38.1 1.5 Acetone 56.2 Infinite Non Azeotropic < 50 ppb Methanol 64.5 Infinite Non Azeotropic < 50 ppb Benzene 80.1 0.18 69.4 8.9 < 50 ppb Toluene 110.8 0.05 85.0 20.2 < 50 ppb -21 Infinite Formic Acid 100.8 Infinite Acetic Acid 118.0 Infinite Pyridine 115.5 57 92.6 43 < 10 ppm Aniline 181.4 3.60 99.0 80.8 < 10 ppm Phenol 181.4 8.20 99.5 90.8 < 10 ppm Nitrobenzene 210.9 0.04 98.6 88.0 < 10 ppm Dimethyl Acetamide 166.1 Infinite Non Azeotropic < 10 ppm n-Methylpyrrolidone 202.0 Infinite Non Azeotropic < 10 ppm Organic Compound Distillation Methylene Chloride Extraction Formaldehyde Non Azeotropic 107.1 Typical Reduction Level < 50 ppb < 1,000 ppm 22.5 Non Azeotropic < 500 ppm < 500 ppm www.modularprocess.com 7 Telephone: (201) 267-8670 Simple Extraction Single Stage MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG A–0 Extract (E) B – 50 C – 0.8 Feed (F) 50.8 A – 99 B–0 A – 99.0 C–1 B–0 100 A–0 C – 0.2 Raffinate (R) B – 50 Solvent (S) 99.2 C–0 50 Fraction Unextracted Distribution Coefficient Extraction Factor Solute in Raffinate 0.2 0.2 Solute in Feed 1.0 0.8 Conc. Solute in Extract 50 7.92 M Conc. Solute in Raffinate 0.2 99 E S M 50 7.92 4.0 F 99 U www.modularprocess.com 8 Telephone: (201) 267-8670 Cross Flow Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG E1 E2 Feed E3 R1 E4 R2 R3 F + S = M1 R1 + S = M2 R2 + S = M3 C C C R4 R3 + S = M4 A+B Solvent Solvent Solvent C B Solvent LEGEND A, B Components in feed C Component in solvent Rx Raffinate from stage x Ex Extract (made up of components B & C) Mx Composition of two phase mixture F R2 A R3 R4 R1 M1 M2 M3 M4 E1 E2 E3 E4 C www.modularprocess.com 9 Telephone: (201) 267-8670 Countercurrent Flow Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG NOTE: Extract is made up of components B and C E1 E3 R2 R1 Feed Solvent C R3 R4 A+B E2 E4 B A Equations F+S=M E1 + R4 = M F + S = E1 + R4 F – E1 = R4 – S = Δ F R1 A E1 M R2 R3 R4 E2 E E3 4 C Δ www.modularprocess.com 10 Telephone: (201) 267-8670 Countercurrent Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG B+C Feed (F) Extract (E): Solute Rich Stream Primary Interface A+B Continuous Phase Dispersed Phase Solvent (S) C Raffinate (R): Solute Lean Stream A www.modularprocess.com 11 Telephone: (201) 267-8670 Bench Scale Test Apparatus MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Variable Speed Drive Baffle Thermometer Tempered Water Out 1 – Liter Flask Tempered Water In Drain www.modularprocess.com 12 Telephone: (201) 267-8670 Simple Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Solute Free Basis Graphical Solution E’ 𝑌𝐵𝐸 F’ 𝑋𝐵𝐹 = 𝑋𝐵𝐹 𝑋𝐴𝐹 S’ 𝑌𝐵𝑆 = 𝑦𝐵𝐹 𝑦𝐴𝑆 + 𝑦𝐶𝑆 𝑦𝐵𝐸 = 𝑦𝐴𝑅 + 𝑦𝐶𝐸 𝑋𝐵𝑅 = R’ YBE 𝑥𝐵𝑅 𝑥𝐴𝑅 + 𝑥𝐶𝑅 Y YBS 𝐹 ′ = 𝐹 𝑥𝐴𝑅 𝑆 ′ = 𝑆 𝑦𝐴𝑆 𝑦𝐶𝑆 𝐸 ′ = 𝐸 𝑦𝐴𝐸 𝑦𝐶𝐸 𝑅′ = 𝑅(𝑥𝐴𝑅 𝑥𝐶𝑅 ) XBR 𝑚= 𝑌𝐵 ∗ 𝑋𝐵 ∗ X XBF Distribution Coefficient on Solute Free Basis www.modularprocess.com 13 Telephone: (201) 267-8670 Typical LLE Equilibrium Curve MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract Comp. (Wt. Frac., Solute Free) 0.09 0.08 0.07 0.06 0.05 0.04 0.03 0.02 0.01 0.00 0.000 0.005 0.010 0.015 Raffinate Composition (Wt. Frac., Solute Free) 0.020 www.modularprocess.com 14 Telephone: (201) 267-8670 Graphical Determination of Theoretical Stages 95% Solute Extraction, S/F = 1.0 mass basis Extract Comp (Wt Frac., Solute Free) MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG (0.136, 0.114) 0.12 0.10 1 0.08 0.06 0.04 0.02 0.00 3 0.000 2 0.020 0.040 0.060 0.080 0.100 0.120 Raffinate Composition (Wt Frac., Solute Free) www.modularprocess.com 15 Telephone: (201) 267-8670 Graphical Determination of Theoretical Stages 98% Solute Extraction, S/F = 1.0 mass basis MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG (0.136, 0.118) Extract Comp (Wt Frac., Solute Free) 0.12 0.10 1 0.08 0.06 0.04 0.02 6 5 0.00 0.000 4 2 3 0.020 0.040 0.060 0.080 0.100 Raffinate Composition (Wt Frac., Solute Free) 0.120 www.modularprocess.com 16 Telephone: (201) 267-8670 Kremser Equation MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG n Where: n xf xn ys m E = = = = = = ys x m 1 1 1 LOG f ys E E xn m LOG E Number of theoretical stages required Conc. of solute in feed on solute free basis Conc. of solute in raffinate on solute free basis Conc. of solute in solvent on solute free basis Distribution coefficient Extraction factor = (m)(S/F) www.modularprocess.com 17 Telephone: (201) 267-8670 Engineering Calculations Kremser Type Plot MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG YBE 1.0 0.8 0.6 E’ E = 0.3 0.4 0.3 F’ XBR/XBF = Fraction Unextracted 0.2 XBF S’ YBS R’ XB E: Extraction Factor E = m (S’/F’) 0.1 0.08 0.06 0.04 0.03 0.02 0.01 0.008 0.006 0.004 0.003 0.002 0.001 0.0008 0.0006 0.0005 1 18 2 3 4 5 6 7 8 10 15 20 Number of Ideal Stages Typical Extraction System MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG B+C+(A) Feed A+B Solvent Recovery Raffinate Stripping Extraction C (A) Solvent C (A+B) A+(B+C) A (B+C) 19 B (C) C (A+B) Removal of Phenol from Wastewater MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract Wastewater Feed 0.1 – 8 % Phenol Solvent Recovery Raffinate Stripping Extraction Recycled Solvent Steam Raffinate < 1 ppm Phenol Biological Treatment Or Carbon Adsorption ppb Phenol Phenol Recovery of Acetic Acid from Water Using a Low Boiling Solvent MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract Aqueous Feed 1 - 30 % Acetic Acid Solvent Recovery Raffinate Stripping Extraction Recycled Solvent Typical Solvents: Ethyl Acetate MTBE Steam Raffinate Acetic Acid Aqueous Raffinate 21 Neutralization/Washing of Acid or Base or Polar Compounds from Organic Stream MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Organic Water Extraction Caustic (Mild)** **Organic Feed could contain caustic. Mid-Feed would be mild acid. Feed (Organic + Acid) ** Water + Salts www.modularprocess.com 22 Telephone: (201) 267-8670 Series Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Feed Extract Solvent 1 B+C C Solvent 2 A+B D Extractor #2 Extractor #1 Raffinate A Extractor 1 & 2 May Differ In: • Temperature • pH • Solvent Product B+D www.modularprocess.com 23 Telephone: (201) 267-8670 Recovery of Caprolactam MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract Lactam Oil Phase 65 – 70% Caprolactam Water Re-Extraction Reaction Section Ammonium Sulphate Phase 2 – 3% Caprolactam Am. Sulphate Ext. Lactam Oil Ext. Feed From Solvent Raffinate AQ Waste to Discharge 24 Am. Sulph. Waste to Discharge Lactam Oil to Recovery Phosphoric Acid Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Recycle Re-Extraction Feed Scrub Extraction Phosphate Rock Digester Extraction HCL Water Scrub Solv. Solvent Raffinate to Disposal 25 Phosphoric Acid to Recovery Organo-Metallic Catalyst Recovery MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Organic Cobalt Catalyst Preparation Extraction Slipstream Feed Organo-Metallic Catalyst Reactor Separator Water Effluent (200 ppm Cobalt) Makeup Organic Water Effluent (1 ppm Cobalt) Product www.modularprocess.com 26 Telephone: (201) 267-8670 Fractional Extraction Process Scheme MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG EI YAE,YBE S I2 XAS2,XBS 2 (A-Rich) NR F1I XAF,XBF NS S 1I XAS1,XBS1 RI (B-Rich) XAR,XBR www.modularprocess.com 27 Telephone: (201) 267-8670 Extraction of Flavors and Aromas MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Typical Products: Orange Oil Lemon Oil Peppermint Oil Cinnamon Oil Aqueous Alcohol Solvent 2 Distillation Solvent 1 Distillation Extraction Essential Oil Hydrocarbon Oil Essential Extract www.modularprocess.com 28 Telephone: (201) 267-8670 Fractional LLE – Mixed Polymer Feed MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG www.modularprocess.com 29 Telephone: (201) 267-8670 Major Types of Extraction Equipment MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Column Contactors Mixer Settlers Used primarily in the metals industry due to: - Large flows - Intense mixing - Long Residence time - Corrosive fluids - History Spray Rarely used Packed Static Tray Centrifugal Agitated Pulsed Used in: - Refining - Petrochemicals Used in: - Refining - Petrochemicals Used in: - Nuclear - Inorganics - Chemicals Example: - Random - Structured - SMVPTM Example: - Sieve Example: - Packed - Tray - Disc & Donut KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. Used primarily in the pharmaceutical industry due to: - Low Volume - Short Residence time - Handles Small Gravity Diff. - History Rotary Reciprocating Used in: - Chemicals - Petrochemicals - Refining - Pharmaceutical Example: - RDC - SCHEIBEL® Example: - KARR® www.modularprocess.com 30 Telephone: (201) 267-8670 Mix / Decant Tank MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Characteristics • Mix – Settle – Phase separate in a single tank • Batch Processing only • Requires multiple solvent additions for more than one stage (crossflow operation) • Typically used for small capacity operations or intermittent processing Feed Inlet Sight Glass www.modularprocess.com Outlet 31 Telephone: (201) 267-8670 Mixer / Settlers MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Characteristics • • Light Phase In • • • Heavy Phase Out • Handle very high flowrates Good for processes with relatively slow reactions (residence time required) Provide intense mixing to promote mass transfer Require large amount of floor space Suitable when few theoretical stages required Large solvent inventory (and losses) www.modularprocess.com 32 Telephone: (201) 267-8670 Centrifugal Extractor MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Characteristics • • • • • • Countercurrent flow via centrifugal force Low residence time ideally suited for some pharmaceutical applications Handles low density difference between phases Provide up to several theoretical stages per unit High speed device requires maintenance Susceptible to fouling and plugging due to small clearances www.modularprocess.com 33 Telephone: (201) 267-8670 Packed Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract (E) Characteristics • Feed (F) • • • • • Solvent (S) Raffinate (R) • High capacity: 20-30 M3/M2-hr (Random) 500-750 gal/ft2-hr (Random) 40-80 M3/M2-hr (Structured) 1,000-2,000 gal/ft2-hr (Structured) Poor efficiency due to backmixing and wetting Limited turndown flexibility Affected by changes in wetting characteristics Limited as to which phase can be dispersed Requires low interfacial tension for economic usefulness Not good for fouling service www.modularprocess.com 34 Telephone: (201) 267-8670 Sieve Tray Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Feed (F) Extract (E) Primary Interface Characteristics • High capacity: 30-50 M3/M2-hr 750-1,250 gal/ft2-hr • Good efficiency due to minimum backmixing • Multiple interfaces can be a problem • Limited turndown flexibility • Affected by changes in wetting characteristics • Limited as to which phase can be dispersed Solvent (S) Raffinate (R) • Not effective for high interfacial tension www.modularprocess.com 35 Telephone: (201) 267-8670 RDC Extractor MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Characteristics • Reasonable capacity: 20-30 M3/M2-hr Drive Motor Gearbox Light Phase Out Heavy Phase In • Limited efficiency due to axial backmixing • Suitable for viscous materials Vessel Walls Shaft Stators Rotors • Suitable for fouling materials • Sensitive to emulsions due to high shear mixing Light Phase In Interface • Reasonable turndown (40%) 36 Heavy Phase Out Interface Control www.modularprocess.com Telephone: (201) 267-8670 SCHEIBEL® Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Characteristics • Reasonable capacity: 15-25 M3/M2-hr 350-600 gal/ft2-hr Variable Speed Drive Light Phase Out Heavy Phase In Rotating Shaft Horizontal Vessel Outer Baffle Walls • High efficiency due to internal baffling • Good turndown capability (4:1) and high flexibility • Best suited when many stages are required • Not recommended for highly fouling systems or systems that tend to emulsify Light Phase In Turbine Impeller Interface Horizontal Inner Baffle Interface Control Heavy Phase Out KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 37 Telephone: (201) 267-8670 SCHEIBEL® Column Internal Assembly MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 38 Telephone: (201) 267-8670 KARR® Reciprocating Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Drive Assembly Light Phase Out Characteristics Heavy Phase Inlet • Highest capacity: 30-60 M3/M2-hr 750-1,500 gal/ft2-hr Sparger • Good efficiency • Good turndown capability (4:1) Perforated Plate Light Phase Inlet Tie Rods & Spacers • Uniform shear mixing Baffle Plate • Best suited for systems that emulsify Sparger Interface Control Interface KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com Heavy Phase Out 39 Telephone: (201) 267-8670 KARR® Column Plate Stack Assembly MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 40 Telephone: (201) 267-8670 Comparing Commercial Extractors MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG 20 SCHEIBEL Efficiency / Stages per Meter 10 6 RZE Graesser KARR PFK 4 PSE RDC 2 1 Key Kuhni FK MS SE .06 0.4 Graesser = Raining Bucket MS = Mixer Settler SE = Sieve Plate FK = Random Packed PFK = Pulsed Packed PSE = Pulsed Sieve Plate RDC = Rotating Disc Contactor RZE = Agitated Cell KARR = KARR® Recipr. Plate Kuhni = Kuhni Column SCHEIBEL = SCHEIBEL® Col. 0.2 1 2 4 6 10 Capacity M3/(M2 HR) 20 40 60 100 KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 41 Telephone: (201) 267-8670 Column Selection Criteria Static Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG A static column design may be appropriate when: • Interfacial tension is low to medium: up to 1015 dynes/cm • Only a few theoretical stages are required, and reduction in S/F is not an economic benefit • No operational flexibility required • There is a large difference in solvent to feed rates www.modularprocess.com 42 Telephone: (201) 267-8670 Column Selection Criteria Agitated Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Agitated columns are generally more economical when: • More than 2-3 theoretical stages are required • Interfacial tension is moderate to high, although low interfacial tensions may also be economical • A reduction in solvent usage is beneficial to the process economics • The process requires a wide turndown as well as the ability to handle a range of S/F ratios www.modularprocess.com 43 Telephone: (201) 267-8670 Column Selection Criteria SCHEIBEL® Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • • • Systems that require a large number of stages due to either theoretical stage requirements or low mass transfer rates Low volume applications in which a relatively small column is required Systems that process relatively easily, without a tendency to emulsify and/or flood KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 44 Telephone: (201) 267-8670 Column Selection Criteria KARR® Reciprocation Plate Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • • • • Difficult systems that tend to emulsify and/or flood easily Systems in which the hydraulic behavior varies significantly through length of the column Sometimes requiring non-metallic internals, such as Teflon due to wetting characteristics or corrosive materials Fouling applications that may have tars formations and/or solids precipitation KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 45 Telephone: (201) 267-8670 3 Cornerstones of Successful Extraction Applications MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Successful Application Proper Solvent Selection Meaningful Pilot Tests Accurate Scale-Up Scale-Up Based on: Selection Based on: Testing Based on: • Sound thermodynamic principles • Sound economic principles • Availability • Recoverability • Sound environmental principles • Toxicity • Safety • Actual feed stocks • Full process including solvent recovery • Wide range of operating conditions • Proven techniques • Proper safety factors www.modularprocess.com 46 Telephone: (201) 267-8670 Solvent Selection MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • Literature – DECHEMA, Perry’s Chemical Engineers Handbook • • Internet search • Experience – consulting with experts • Laboratory Experiments: Understanding the chemistry of the process 1. Quickly screen solvents 2. Generate equilibrium data 3. Observe phase behavior www.modularprocess.com 47 Telephone: (201) 267-8670 Liquid-Liquid Extraction Scale-Up MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Theoretical scale-up is difficult due to Complex processes occurring in an extractor • Coalescing / Wetting Characteristics • Interfacial and Drop Turbulence Effects • Axial and Radial Mixing • Tendency to Emulsify • Phase Ratio Variability and Density Gradients • Effects of Impurities or Solids • Mass Transfer Rate www.modularprocess.com 48 Telephone: (201) 267-8670 Liquid-Liquid Extraction Scale-Up MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Best method of design: Pilot testing followed by empirical scale-up www.modularprocess.com 49 Telephone: (201) 267-8670 Pilot Plant Configuration MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Determine type of column to be used based on process considerations Use the same kind of equipment for the production unit Determine diameter and height of pilot column based on experience Table 1: Smallest Possible Column for Testing Type of Column Packed Tray Diameter 3” to 4” ≥ 6” Height 3’ to 6’ per Theoretical Stage (TS) 4 to 5 Trays per TS KARR® 1” 1’ to 3’ per TS SCHEIBEL® 3” 3 to 6 Actual Stages per TS (Approx. 3” to 6”) KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 50 Telephone: (201) 267-8670 Continuous Extraction Pilot Plant Arrangement MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Extract Hot Oil Raffinate Feed Solvent www.modularprocess.com 51 Telephone: (201) 267-8670 KMPS Pilot Plant Services Group MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG KMPS maintains a pilot plant dedicated to extraction R & D and applications testing www.modularprocess.com 52 Telephone: (201) 267-8670 Which Phase is Continuous? MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Solvent is Light Phase B+C E F F Primary Interface A+B Solvent Dispersed S Solvent is Heavy Phase A+B Solvent Continuous S C A A S E B+C R Primary Interface F A+B R A A S Solvent Dispersed C R C Primary Interface R C Primary Interface Solvent Continuous F A+B E B+C E B+C www.modularprocess.com 53 Telephone: (201) 267-8670 Determining the Dispersed Phase MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Flow Rate (Phase Ratio) • For Sieve Tray and Packed Columns – disperse the higher flowing phase • For Agitated Columns – disperse lower flowing phase Viscosity • For efficiency – disperse less viscous phase Viscous drop Diffusion rate inside the drop is inhibited by viscosity • For capacity – disperse more viscous phase Viscous continuous phase Drop rise or fall will be inhibited www.modularprocess.com 54 Telephone: (201) 267-8670 Determining the Dispersed Phase MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Surface Wetting • Want the continuous phase to preferentially wet the internals – this minimizes coalescence and therefore maximizes interfacial area. Droplets coalesce. Interfacial area lost. Droplets retain shape. Maximizes interfacial area. Importance of maintaining droplets Assume – 30% holdup of dispersed phase in 1 M3 of solution Droplet Droplet Diameter [m] Volume [M3] Number Droplets Droplet SA [M2] Interfacial Area [M2/M3] 100 0.3 7.16x1010 1.26x10-7 9022 300 0.3 2.65x109 1.13x10-6 2995 500 0.3 5.73x108 3.14x10-6 1796 www.modularprocess.com 55 Telephone: (201) 267-8670 Determining the Dispersed Phase MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Marangoni Effect • Coalescence is enhanced by mass transfer from droplets continuous phase Mass Transfer Direction C A+B A+B C A+B C+B Continuous c) • Droplets tend to coalesce • Must be counteracted by additional energy A C Dispersed (d C+B Continuous (c Dispersed d) • Droplets tend to repel each other • Less energy required to maintain dispersion www.modularprocess.com 56 Telephone: (201) 267-8670 Interface Behavior MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Solids build up at the interface = Rag Layer Rag Layer Emulsion band builds up at interface due to slow phase separation Rag Layer www.modularprocess.com 57 Telephone: (201) 267-8670 Rag Layer or Emulsion Band MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Corrective Action 1. Reverse Phases 2. For Emulsion Band: slow down capacity or reduce agitation speed 3. For Rag Layer: circulate liquid through an external filter Filter Feed www.modularprocess.com 58 Telephone: (201) 267-8670 Entrainment MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Entrainment refers to removing a small portion of one phase out of the wrong end of the column i.e. where the other phase exits. Entrainment is controlled by: 1.) Increased settling time inside the column 2.) Coalescer inside the column 3.) Coalescer external to the column E E E E F 1 S F F F OR 2 OR S S S 3 R R R R www.modularprocess.com 59 Telephone: (201) 267-8670 Flooding MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Flooding – the point where the upward or downward flow of the dispersed phase ceases and a second interface is formed in the column Flooding can be caused by: • Increased continuous phase flow rate which increases drag on droplets f Primary Interface F2 > F1 f Primary Interface E E F1 F2 Second Interface S S R R www.modularprocess.com 60 Telephone: (201) 267-8670 Flooding MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Flooding can be caused by: • Increased agitation speed which forms smaller droplets which cannot overcome flow of the continuous phase • Decreased interfacial tension – forms smaller drops – same effect as increased agitation f1 Primary Interface f2 > f1 f2 Primary Interface E E F1 F2 Second Interface S S R R www.modularprocess.com 61 Telephone: (201) 267-8670 Pilot Plant Testing MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Column Selection Based Upon: 1. Process Criteria 2. Physical/Chemical Properties 3. Laboratory Work 4. Experience Test Method 1. Experimental Design 2. Step-by-Step Optimization www.modularprocess.com 62 Telephone: (201) 267-8670 Agitated Column Testing MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • • Set-up column (multiple inlets) • Select initial operating conditions (capacity – S/F – No. Stages) • Operate at increasing agitation speed (flooding) • Based on results, vary: Select continuous and dispersed phases 1. Continuous phase 2. S/F vs No. Stages 3. Capacity 4. Other Variables (temp, pH, etc.) www.modularprocess.com 63 Telephone: (201) 267-8670 Static Column Testing MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • • Set-up column (multiple inlets) • Select initial operating conditions (capacity – S/F – height) • • Operate 3 different capacities Select continuous and dispersed phases Based on results, vary: 1. Continuous phase 2. S/F vs Column Height 3. Other Variables (temp, pH, etc.) www.modularprocess.com 64 Telephone: (201) 267-8670 Extractor Flow Patterns MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Ideal Plug Flow Y Actual Flow Y X X This “axial” or “back” mixing causes concentration gradients that decrease driving force and therefore increase HETS www.modularprocess.com 65 Telephone: (201) 267-8670 Generalized Scale-up Procedure MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Pilot Scale f2 f1 Q2 Q1 Feed Rate Feed Rate H1 D1 Basic Scale-up Relationships: D2/D1 = K1(Q2/Q1 )^M1 H2/H1 = K2(D2/D1 )^M2 f2/f1 = K3(D2/D1)^M3 D2 Where: K1, M1 = Capacity Scale-up Factors K2, M2 = Efficiency Scale-up Factors K3, M3 = Power Scale-up Factors www.modularprocess.com 66 Telephone: (201) 267-8670 Application – SCHEIBEL® Column MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • Extraction of nitrated organics from spent acid stream using an organic solvent • Reduce nitrated organic compounds from 3.9% to less than 50 ppm • S/F ratio fixed by process at 3.9 • Equilibrium data indicated that 4.5 theoretical stages required KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. www.modularprocess.com 67 Telephone: (201) 267-8670 SCHEIBEL® Column Pilot Plant Setup Nitrated Organics Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Interface Variable Speed Drive Hot Oil Organic Extract Spent Acid Feed Aqueous Raffinate MCB Solvent www.modularprocess.com KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. 68 Telephone: (201) 267-8670 SCHEIBEL® Column Nitrated Organics Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Column designed based upon results from the pilot plant tests: D1 A B •Diameter = 14” (D1) • Expanded Head Diameter = 20” (D2) • Bed Height = 9’-6” (A) • Overall Height = 16’-4” (B) D2 www.modularprocess.com 69 Telephone: (201) 267-8670 Application 2 - Recovery of Carboxylic Acids from Fermentation Broth MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Broth generated from cellulosic materials – approx. 5% acids LLE Goal: To achieve >95% recovery (high purity) and minimize solvent usage Ethyl acetate selected solvent – but emulsified easily Preliminary Data in RDC Columns Difficult operation due to emulsification < 90% acid recovery High S/F ratio – 2.0 KARR® Column Required www.modularprocess.com 70 Telephone: (201) 267-8670 Pilot KARR® Column for Carboxylic Acids 1” diameter x 12’ Plate Stack MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Variable Speed Drive Organic Out (Extract Phase) Hot Oil Aqueous Out (Raffinate) Whole Broth Feed Ethyl Acetate www.modularprocess.com 71 Telephone: (201) 267-8670 Results from Extraction Testing MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • Process successfully tested in KARR® Column and data generated for scale-up • KARR® Column is the correct design for this process which failed in RDC column • S/F ratio improved to 1.5 (client expected 2) • 96-97% recovery at room temperature and 98-99% recovery at 40-45 C • Complete system (LLE + distillations) designed, fabricated, and installed • LLE testing identified “unknown” component www.modularprocess.com KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. 72 Telephone: (201) 267-8670 KARR® Column Design Carboxylic Acid Extraction from Broth MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • Diameter = 22” (D1) • Expanded Ends Diameter = 44” (D2) • Plate Stack = 38’-0” (A) • Overall Height = 50’-6” (B) D1 A B D2 www.modularprocess.com Telephone: (201) 267-8670 Application - Aromatic Purification by Fractional Liquid-Liquid Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG •Light tar feed with polar aromatics (product) and non-aromatic impurities •>90% recovery; 1% impurities •Polar solvent for aromatics •Alkane for non-polar impurities •Preliminary Data in RDC Columns Many extraction stages High ratio of non-polar to polar solvent Significantly more non-polar solvent stages required www.modularprocess.com 74 Telephone: (201) 267-8670 PFD - Pilot Plant Setup: Aromatic Purification by Fractional Extraction MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Stage 99 Stage 77 Stage 65 Stage 53 Stage 42 Mixed Polar Solvent Organic Feed Non-Polar Solvent (Alkane) Stage 0 Extract Raffinate www.modularprocess.com 75 Telephone: (201) 267-8670 Fraction Extraction Test Variables MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG • • • • 65-99 agitated stages 12-34 stages above feed 42-65 stages below feed Capacity 21 – 25.5 m3/m2 hr • • • Polar solvent to feed ranged between 0.5: 1 and 1.4 : 1 Non-polar solvent to feed ranged between 1.1:1 and 3:1 Agitation speed 400-850 RPM www.modularprocess.com 76 Telephone: (201) 267-8670 Aromatic Purification Final Results – Design Basis MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Scale-up design: Diameter 1778 mm (70”) Height 65 Agitated stages Feed Stage 13 from top Polar solvent: Feed 0.7: 1.0 Non-Polar: Feed 1.8: 1.0 Internals = Variable Impeller Diameters 94% recovery with <1.0% impurities www.modularprocess.com 77 Telephone: (201) 267-8670 www.modularprocess.com Telephone: (201) 267-8670 MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG Alcohol Extraction from Acrylates Extraction of methanol from an acrylate stream using water as the solvent Reduce methanol from 2.5% to less than 0.1% S/F ratio specified by client as 0.32 wt. basis Equilibrium data: distribution coefficient generated by KMPS, with average value of 5.3 78 KARR® Column Pilot Plant Setup Alcohol Extraction from Acrylates KARR® Column 1” Dia. x 8’ Plate Stack Variable Speed Drive Variable Plate Spacing Hot Oil Raffinate (Acrylate Phase) Water Feed Extraction Technology Group www.modularprocess.com Extract (H2O + Alcohol) Acrylate Feed (methyl or ethyl) Interface KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. KARR® Column Pilot Plant Scale-up Methanol Extraction from Acrylate • Diameter = 45” (D1) • Expanded Head Diameter = 68” (D2) • Plate Stack = 26’-0” (A) • Overall Height = 36’-8” (B) D1 A B D2 Extraction Technology Group www.modularprocess.com KARR® and SCHEIBEL® are registered trademarks of Koch-Glitsch, LP. Extraction Experience MO D U L A R P R O C E SS S Y S T EMS | D I S T I L L ATI O N | L I Q U I D E XT R A C T I O N | E N G I N EER I NG | P I L O T T E S T I NG KMPS has supplied over 300 commercial extraction columns KMPS has also supplied hundreds of pilot scale extraction columns We have tested more than 200 different processes in the pilot plant QUESTIONS? www.modularprocess.com 81 Telephone: (201) 267-8670