092710 SepUnitOps

092710 SepUnitOps - as $2.: 5G,... 231% E .2 .3: E E. Em:...

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Emfl mini: flaw: E 53 mfixnflm .flm.._.HEEEE Sn, JEEEU Em 55:“ En mmfihu 1% 5: $352 an. Eufiam E: E1— :wmm—H ELK:th HE: TeammH Hubs: 5: Eu: Tam—H 5?: EH. HE: FHEmmfl mEHmEnEm man... 2%: 23m Can 5.. EH: 33m H as? 33E E HE E HUME EU Esq: Efim Emma, 23: E. :31. EEE Human— .5 EE. -I-i fluimanfl 2m? .flafim Eu. mflzflmfinfl :mfimfln E 2 2252355: sac.”— H H: H EEHuEHHu EETEEHH 3:35 E HH :EHHHEHHEHED A...“ H H :EHEHHHEFDU :1 H cEEHomFHrm— 22F: an. HHEHEEnFm EEEH_.E_..G,H fl; BEE. Table 1.2 Separation lCllperations Based on a Barrier Separation [nitial or Clpe ration E.'_Ir'rnbol“I Feed Phase Dsmosis {1] ED Liquid Reverse osmosis” {2] I L Liquid L Dialysis [3] L L Liquid L Mierofiltration [vi] 1. Liquid L I. Ultrafiltration {5} Liquid Peryaporation" as] L 15- Liquid 1-" Gas permeation” {7] l" V 1iir’apor 1r. Liquid membrane [3] ma W!- 1iit"apor andfor liquid WL '[lesign procedures are fairly well accepted. ‘ISingle units are shown. Multiple units can be easeaded. Separating Agent blonporous membrane blonporous membrane with pressure gradient Porous membrane with pressure gradient Mieropo rou s membran e wit h p ressu re g rad ie nt Mieroporou s membran e wit h p ressu re g radie nt Non porous membrane with p ressu re g rad ie nt blonporous membrane with pressure gradient Liquid membrane Wltll pressure gradient [ndustrial Example!“ Desalinization of sea 1Hater [yo]. 24, pp. 349—353] Recovery of eaustie froiu liemieellulose [Yo]. ’1', p. 5T2] Removal of bacteria from drinking water [i’o1.15_.p.115] Separation of whey froiu eheese [info]. 15, pp. Edi—5M] Separation of azeotropio mi ntures [ya]. 15. pp. [to—1th Hydrogen enrieh meitt [Vol. 21:}. pp. "11:19—31 1D] Removal of ltydrogen sulfide [Vol.15_.p. 119] bCitations refer to volume and pagers] of Kt'rk—flrftmer Ertq'efopedfn of Chemical Teehnologjg 3rd ed._. John Wiley and Sons. New York [HITS—l 934-]. Table 1.3 Separation lCilperatiotts Based on a Solid Agent Separation lnitial or Separating Industrial Operation Symbol“ Feed Pliase Agent Eaantple'i Adsorption" {l ] Wu W!— 1Vapor or liquid Solid adsorbent Purification of p-aylette Wol. 1-4, pp. TEE—3'25} WI. Chmmmflgmphgn [E] m Vapor or liquid Solid adsorbent or Separation of xylene iso— liquid adsorbent oit nters and etbylbenzette a solid support Wol. 14, pp. Fifi—3'2?) m [on exchange" {3}: L .t. Liquid Resin with ion—active sites Detnitteralization of water i‘r’ol. 13, pp. TDD—TM} —I- I. 'Design procedures are fairly.r well accepted. ETSirtgle units are shown. Multiple units can be cascaded. bCitations refer to 1roiun'te and pagers} of Kirk—49mm er Eng-riopedéo offlhrmir‘oi ii'r'r'ii'rti-_'.It‘og_t:= 3rd ed_, John Wiley and Sorts. New York tIWS—i SIB-4,1. Table 1.4 Separation lCllperations by Applied Field or lCradient Separation initial or Force Field or industrial lClperation Feed Pitase C-radient Esatnple‘” Ceatrifugatioa {l} lt’apor Centrifugal force fteld Separation of uranium isotopes i‘i’ol. 23. pp. 531—532} Thertnal diffusion {E}: Vapor or liquid Tltertttal gradient Separation of cltloriae isotopes [Yo]. "I. p. fiSri} Electrolysis {3] Liquid Electrical force field Concentration of iteatr}r 1«rater [Rio]. 1p. 55D} Electrodialysis [4} Liquid Electrical force field and Desalinization of sea 1«rater membrane [Vol. 14. pp. SSS—359} Electrophoresis [5} Liquid Electrical force field RECUVEI‘}' of ltetniceilttioses [Yo]. 5., p. 551} Field—flow fractionation to] Liquid Latnittar flow in force field “Citations refer to 1aoluo'te and pagers} of Kirk—Dram er Enq'rfopea'r'a rngftemi'cat‘ Tfl'hnologjq 3rd ed.. John Wiley and Sons. New York HE'S—1934}. ...
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This note was uploaded on 12/29/2011 for the course CHE 128 taught by Professor Scott,s during the Fall '08 term at UCSB.

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092710 SepUnitOps - as $2.: 5G,... 231% E .2 .3: E E. Em:...

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