1 / 26

evoparation

evoparation

shivaram
Download Presentation

evoparation

An Image/Link below is provided (as is) to download presentation Download Policy: Content on the Website is provided to you AS IS for your information and personal use and may not be sold / licensed / shared on other websites without getting consent from its author. Content is provided to you AS IS for your information and personal use only. Download presentation by click this link. While downloading, if for some reason you are not able to download a presentation, the publisher may have deleted the file from their server. During download, if you can't get a presentation, the file might be deleted by the publisher.

E N D

Presentation Transcript


  1. EVAPORATION HEAT TRANSFER COEFFICIENTS AND SINGLE EFFECT EVAPORATORS By T.Shivakumar B.Pharmacy Shiva.pharmacist@gmail.com

  2. PROCESS DESCRIPTION • OBJECTIVES • CONCENTRATE SOLUTE • RECOVER SOLVENT • FORM CRYSTALS • MECHANISM • HEAT EXCHANGE WITH PHASE CHANGE • BATCH OR CONTINUOUS http://www.niroinc.com/html/evaporator/rising_film_evaporators.html

  3. DESIGN FACTORS • SOLUTION FLUID VISCOSITY • HEAT TRANSFER COEFFICIENTS • PRESSURE DROPS • SOLUTE SOLUBILITY • SUPERSATURATED CONDITION • MATERIALS (BIO-MATERIALS) MAY BE HEAT SENSITIVE • DEGRADATION TEMPERATURE • ELEVATED PRESSURE • BOILING POINT ELEVATION http://www.aai-csi.com/images/evaporator.jpg

  4. EVAPORATION DESIGN FACTORS • HIGH TEMPERATURE REACTIONS • FOAMING • SCALING AND CORROSION http://www.aquasant-mt.com/Foam.159.0.html?&L=1 http://www.champ-tech.com/images/products/pipe.jpg

  5. OTHER DESIGN FACTORS • SPECIFIC HEAT • HEAT OF CONCENTRATION • FREEZING POINT VS. CONCENTRATION • GAS LIBERATION • TOXICITY • EXPLOSION HAZARDS • NEED FOR STERILITY

  6. EVAPORATION COMPARED WITH DISTILLATION • SOLUTE IN EVAPORATION IS GENERALLY NON-VOLATILE, RELATIVE TO SOLVENT http://www.novasep.com/technologies/img/evaporation-graph2.gif http://www.schoolscience.co.uk/content/4/chemistry/petroleum/knowl/images/still.jpg

  7. EVAPORATION EQUIPMENT • SUMMARIZED IN FIGURE 8.2-1 http://www.niroinc.com/html/evaporator/esys.html

  8. EVAPORATION EQUIPMENT • FORCED CIRCULATION AND RECOMPRESSION UNITS http://www.niroinc.com/html/evaporator/esys.html

  9. EVAPORATOR EQUIPMENT • PLATE & FRAME - CRYSTALLIZERS http://www.niroinc.com/html/evaporator/esys.html

  10. OSLO TYPE CRYSTALLIZERS http://www.niroinc.com/html/evaporator/esys.html

  11. OTHER CRYSTALLIZERS http://www.niroinc.com/html/evaporator/esys.html

  12. THIN FILM EVAPORATORS • USED FOR VISCOUS AND THERMALLY SENSITIVE MEDIA http://www.artisanind.com/documents/pa_lecithin.pdf

  13. INTEGRATED PLANT http://www.niroinc.com/html/evaporator/flash-ppt/VMPfcopy1.html

  14. EVAPORATOR CONFIGURATION • SINGLE STAGE EVAPORATORS • HEAT TRANSFER

  15. MULTI-EFFECT EVAPORATORS • STEAM FROM ONE EFFECT IS THE HEAT SOURCE FOR THE SECOND EFFECT http://www.nukem.de/global/downloads/englisch/Evaporation.pdf

  16. MULTI-EFFECT COUNTERFLOW CONFIGURATION • FIGURE 8.2-3 FEED-FOREWARD • PRESSURE IS REDUCED IN EACH STAGE • FEED & STEAM ENTER THE SAME STAGE IN THE TRAIN • FIGURE 8.2-4 – FEED-BACKWARD • PRESSURE IS INCREASED IN EACH STAGE • FEED & STEAM ENTER FROM OPPOSITE ENDS OF THE TRAIN

  17. PARALLEL FEED • SOLAR EVAPORATION SYSTEM http://www.rio5.com/proceedings/Solar/da_Silva_et_al_201-206.pdf

  18. EVAPORATOR HEAT TRANSFER • OVERALL HEAT TRANSFER COEFFICIENTS – SEE TABLE 8.3-1 • NEED TO KNOW RANGE TO REVIEW QUOTED DESIGNS • NOTE THAT PLATE & FRAME CAN HAVE HIGHER COEFFICIENTS THAN SHELL & TUBE.

  19. CHANGE OF PHASE HEAT TRANSFER • SECTION 4.8 FOR SUMMARY OF MECHANISMS • FIGURE 4.8-1 • CONVECTION • NUCLEATE • TRANSITION • FILM http://www.scielo.br/img/revistas/jbsmse/v27n1/25372f10.gif

  20. HEAT TRANSFER COEFFICIENTS • BASED ON ΔT

  21. OTHER CORRELATIONS • FOR EACH CONFIGURATION • PERRY’S PAGE 5-22 • HANDBOOK • http://www.wlv.com/products/databook/ch5_3.pdf • CONVECTIVE BOILING IN COILED TUBES • http://www.graham-mfg.com/downloads/12.pdf • BASED ON SURFACE • http://www.energy.kth.se/index.asp?pnr=10&ID=125&lang=0

  22. SINGLE STAGE MODELS • MASS AND ENERGY BALANCES

  23. MASS & ENERGY BALANCES • COMPONENT MASS BALANCE • SYSTEM HEAT BALANCE

  24. OTHER DESIGN FACTORS • LOWER EVAPORATION PRESSURE • WILL INCREASE EFFECTIVE ΔT • LOWER EVAPORATOR AREA • INCREASED SOLVENT CONDENSER AREA • HIGHER VELOCITIES MIST ELIMINATION • BOILING POINT ELEVATION • REDUCES EFFECTIVE ΔT WITH INCREASING CONCENTRATION

  25. BOILING POINT ELEVATION • DÜRING’S RULE – SOLUTION BOILING POINT IS LINEARLY RELATED TO PURE WATER NBPt AT PSYS • FIGURE 8.4-2 http://www.nzifst.org.nz/unitoperations/unopsassets/fig8-3.gif

  26. ENTHALPY-CONCENTRATION • HEAT OF MIXING EFFECTS • NON-IDEAL Dharmendira Kumar, M.; Ashok Kumar, P.; Rajendran, M., Salt Effect on the Enthalpy of Mixing of 1,4-Dioxane + Acetic Acid at 303.15 K , J. Chem. Eng. Data; (Article); 2003; 48(6); 1422-1424.

More Related