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Liquid holdup in packed columns PDF

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LIQUID HOLDUP IN PACKED COLUMNS A Thesis Presented to the Faculty of the School of Engineering The U niversity of Southern California In P a rtia l Fulfillm ent of the'Requirements for the Degree Master of Science in Chemical Engineering by Richard E. Melrose June 1950 UMI Number: EP41731 All rights reserved INFORMATION TO ALL USERS The quality of this reproduction is dependent upon the quality of the copy submitted. In the unlikely event that the author did not send a complete manuscript and there are missing pages, these will be noted. Also, if material had to be removed, a note will indicate the deletion. Dissertation Publishing UMI EP41731 Published by ProQuest LLC (2014). Copyright in the Dissertation held by the Author. Microform Edition © ProQuest LLC. All rights reserved. This work is protected against unauthorized copying under Title 17, United States Code ProQuest LLC. 789 East Eisenhower Parkway P.O. Box 1346 Ann Arbor, Ml 48106- 1346 This thesis, written by Richard E. Melrose under the guidance of hi.s.... Faculty Committee, and approved by all its members, has been presented to and accepted by the Council on Graduate Study and Research in partial fulfill­ ment of the requirements for the degree of Master of Science in Chemical Engineering Date Faculty Committee I Chairman 'jgL&aMe*L SUMMARY The liquid holdup in packed columns was inves­ tigated using four different packings, three liquids, and two sizes of columns. The investigation was di­ vided into a study of the liquid which wets the pack­ ing (static holdup) and the liquid which is in the voids of the packing under operating conditions (oper­ ating holdup). Static holdup was found to be dependent on the packing m aterial to a large extent. With packing which is non-absorbent and is completely wet by the liquid, static holdup for liquids and packings used in th is in­ vestigation may be expressed by the equation: Hs r 0.029( /i2 S/ r yo g0)*°74 With absorbent packing, most of the sta tic hold­ up may be liquid absorbed in the packing m aterial and w ill depend on the porosity of the m aterial. If the packing surface is liquid repellent, drops w ill collect on the surface and in the crevices, and the above equa­ tion does not apply. Operating holdup was found to follow the equation: H0 r KL’f where K and f are functions of the packing and liquid being used. Operating holdup is independent of the liquid disperser, and is not affected by repacking the column. Increasing the size of the packing or re ­ ducing the column diameter reduces operating holdup. When foaming occurs, operating holdup increases and does not follow the above equation. TABLE OF CONTENTS CHAPTER! PAGE I. INTRODUCTION.......................................................... 1 The problem ........................................ . . 1 Statement of the problem . . . . • 1 Importance of the s tu d y ......................... 2 Definitions of terms u s e d ........................ 4 II. REVIEW OF THE LITERATURE............................. 7 General r e v i e w ................................................ 7 Relation to absorption rate .................... 8 Effect of gas v e l o c i t y ............................. 11 Effect of column d ia m e te r........................ 11 S tatic holdup ..................................................... 12 Holdup in packed d istilla tio n columns 12 Theoretical considerations .................... 13 I II. EXPERIMENTAL WORK ........................................... 14 Apparatus .............................. 14 Operating holdup .................................. 14 Static holdup ............................................ 18 M aterials . . . . . .................................. 19 Liquids . . . ....................................... 19 Packings ..................................................... 22 Measuring devices .................................. 22 Experimental procedure ............................. 28 V CHAPTER PAGE Static h old u p .................................................... 29 Absorption of liquid by the packing .......................................................... 30 IV. EXPERIMENTAL RESULTS................................... 31 Effect of liquid d isp ersers.................. y £ E ffect of operating time on steady-state operation ........................ 33 Effect of column d iam eter.......... 33 Effect of repacking the column . . . 33 D istinguishing between operating and static h old u p ....................................... 33 Static holdup . ....................................... 49 Discussion of experimental methods .......................................................... 52 Static holdup results .................................. 33 Operating holdup ........................................... 59 Variables considered .................................. 59 Operating holdup resu lts ........................ 6l Effect of foam ing............................. 69 Effect of packing size and shape . . 72 V. SUMMARY AND CONCLUSIONS................................ 73 NOMENCLATURE............................................................................. 73 CHAPTER PAGE BIBLIOGRAPHY.................................................... 81 APPENDIX A. Sample c a lc u la tio n s ....................... 83 APPENDIX B. Experimental data and LIST OF TABLES TABLE PAGE I. Liquid Physical P r o p e r t i e s .......................... 23 II. A. S. T. M. D istillatio n of the K e ro s e n e .................................................... 24 III. Packing Properties ............................................. 25 IV. Effect of Operating Time on stead y-state...................................... 34 V. Effect of Viscosity on T0 .............................. 48 VI. Static Holdup Summary .................................... 56 VII. Operating Holdup Equation Constants .......................................................... 68 VIII. Operating Holdup Sum m ary............................. 73 LIST OF FIGURES FIGURE PAGE 1. Results of Other I n v e s t i g a t o r s .............................. 10 2. Schematic Diagram of Operating Holdup Equipment ......................................................................... 1.5 5* Photograph of Operating Holdup Equipment ......................................................................... 17 4. Schematic Diagram of S tatic Holdup Equipment ......................................................................... 20 5* Photograph of S tatic Holdup Equipment . . . . 21 6. Photograph of the Packings U s e d .............................. 26 7. Effect of Liquid Dispersers on Operating H o ld u p .......................................................... 22 8. Drainage Rate of Water from l/2" Raschig Rings ............................................................... 37 9. Drainage Rate vs. Adjusted Time ......................... 27 10. Drainage Rate of Water from 1” Raschig Rings ............................................................... 39 11. Drainage Rate vs. Adjusted T im e.............................. 39 12. Drainage Rate of water from 1-1/2” Raschig Rings ............................................................... 40 12. Drainage Rate vs. Adjusted Time ......................... 40 14. Drainage Rate of Water from 1” Berl Saddles . . . . . . . . . . . . . . . 41

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