Sierface Chemistry Vishal Tiwari Sikkim • occurs only at Adsoon Adsorbate Adsorbent : ! : - : accumulation - at the bulk . not in of species at surfaces Édiq ) Substance which accumulates Material - c - surface is not on which accumulation occurs Removal of adsorbate from adsorbent . . bulk . Adsorptioninaetione Cig 04^12 , C' 214th 502 add _÷÷ii dt÷ charcoal pyessnr Pressure is bcoz Iii , - É charcoal color Solution ofdye C. methylene blue) adsorption of gases add reduced on charcoal takes place . 'M colorless molecules of adsorbed surface . due on of charcoal . . ( Iii , aq Sol of raw sugar ( color) # Air becomes dry in %, colorless charcoal presence of silica gel ( . water molecule ) gets adsorbed on silica gel . aHn . Surface phenomena Concentration absorbplion . of adsorbate increases only at surface and ex : - . dipped in ink Suddenly taken out chalk S * not in bulk water vapour is adsorbed by silica gel # Rate is high in beginning $ decrease till eqm . / Bulk / "" / water 1 phenomena . uniformally distributed throughout body of material adsorbate is . Chalk 9 dipped in ink for long period of time a vapour is absorbed cacti by anhydrous Rate remains constant throughout the process . - Sorption : Adsorption § absorption take place ¥É÷÷÷""%%n tool 0000 188-0708 0000 01000 1¥09 100010 I-iunbalancedresidudfofr-nel.io . 88%880 I Bulk particle → force is surface particle lfnet -107 balanced To make fnet.no adsorption occurs . adsorption is • • Due to an exothermic process ( AH . = - adsorption movement of gas particles entropy decreases ) Ds=-Ve__ /DG=DH-TAs-| Ah Fe = = attraction reduces AS -= . . ve - - re AG- (TAS) C- vet AH 1- high value For ) ↳ AH = - spontaneous process ve • spontaneous process AH should have high - re value . ☐ G= AH 1 f. - T highly spontaneous TAI tire - re { initially after sometime after longtime AH > Toss rapid → adsorption ☐ H=TAS → ☐ H< TAS Eqm : desorption physi sorption Chemisorption - ( physical adsorption) ( chemical adsorption) Vanderwall force btw • • chemical bond ( ionic/ covalent) btw adsorbates adsorbent adsorbates adsorbent • St requires high Energy of activation ( activated adsorption ) . • gt is not → a specific given surface any in nature does . not show preference for - a gas to be adsorbent - St is • • 9T highly specific in occurs only if chemical bonds formed a are nature . → Reversible → more adsorption takes place when premiere increased → • since it is • is exothermic process . temp is favorable at high temp adsorption (physical) Low St required high Energy of activation . a lrreresibleo . decreases lechatelie-n.ci/o1e . . ÷⇐ adfor lowtempis favorable Temp tliqhtempis favorable . gt depends on nature of gas easily liquefiable gas more adsorbed 9 1- also . depend nature are on of gas e gains which . . form bond shows chemisorption chemical or gases with high critical is easily adsorbed temp . . Enthalpy of adsorption 120-40 more gf is surface / KJ Mot area more multilayered → . 80-240 ktlmof ) adsorption → → more surface unilayered . area more chemisorb't Adsorptionisotherm → shows of gas adsorbed amount with pressure /Temp const) Freudlichisotherm of adsorbed mass gas c- Im = P "" \ ( M" K 't adsorbent pressure k , n → depends on const ( nature of : ÷"÷ i 249K adsorbates adsorbent) low pressure moderate high i' pressure region n : : - 021,21 - region t.p-N-m-kpyr.mn ! - nt=0 nm_=kpYn Im = const . ÷ Take : log §m) Kp "n both sides c. + M R logktn-logphogf .KZ/ickhc=iogxI- - - -i -.#logp log = Adsooptionfromsolwhionphase % log Im = K = E. [ og log Yn + K "" In log [c) / L " loge remain Promoters : unchanged → called do → opposite of $ themselves catalysis process is . substance which enhance Haber 's Prom Poison tioh the rate accelerate Nz 1- 3112 Promoter - activity of ¥0s 2MHz a called catalysis catalyst . . Homogenous Catalyst Reactant and : catalyst both insane phase 25021-02 (g) " 2503cg ) . cg) ( ttscooctlz ce ) ( 1214272011 Heterogeneous catalyst ¥ 2502¥ 02 t 02 MHz Vegatable fate , ,, , + 1- Hzocey ( ag ) 1- H) 1120 ( y) CH, Coon Ñ ( c. Hizb Hz (9) 1- can _É 2503cg ] É +413017 NO 1- Glucose 1420 Nisvegatableghell CGHIZOG eaa ) fructose . Adsosptiontheoryoftleterogenouscatalyst ① Diffusion of reactant to the ② Adsorption of reactant ③ Reactant molecules combine on surface of catalyst catalyst Iz ← 'I / . ④ Desorption of Products ⑤ catalyst is again available for farther occurs - , PM . ¥ catalystsbowseetivity city 1- H2O co + Hz É HCO Carson crz 03 Enzymecatalyst Complex nitrogenous organic compound fproteins Biochemical catalyst lnversionofcanesugar 42 Hzz 011µg , 1- H2O É CGH ,20g 1- CGH, 20g Glucose glucose-s.ge?,YffY#zymase-2czHs-on1- 202 fructose . starch I%ialtose 2(CoHio0s)n €1T starch Maltose maltase 421122011 maltose . - glucose ( 12112201 , . ← (6171206 = milk És protein card ne peptide protein -÷÷o amino acid . . mechanism steps E + ⑨ s key lock mechanisms ⑤ → 1991 + → EP → Et p . Haber's process Ostwald process Contact Decor Bosch is ,, Fe, Cmo ) → → → → → " Pt V05 Cuclz fezOztCK03 catalyst eat { u,q--