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IndianJournalof En~neering& MaterialsSciences Vol. 3, December1996,pp. 243-247 , '" -, Reductive dissolution of hematite in hydrochloric acid medium by some inorganic and organic reductants: A comparative study KMParida&NNDas RegionalResearchLaboratory(CSIR),Bhubaneswar751013,India Received18April 1996;accepted6 September1996 Dissolution behaviourof naturally occurring hematite(> 97% Fe203)in hydrochloric acid medium with or without the presenceof reductantshas beeninvestigatedas a function of acid concentration, temperature,liquid/solid ratio, reductant concentrationand particle size. FeCl2 and SnCl2 are found as the best reductants among all the organic and inorganic reductants.Addition of FeCl2 or SnCl2to the extentof 2 wt % enhancesthe formation of Fe2+ in the solution which in turn increases the percentageof dissolutionand alsolowersthe time of dissolution(> 90%)from 6 to 3h. The dissolution of iron oxides is an important chemical reaction that takes place in several fields of chemistry, viz., leaching of oxide ores in hydrometallurgy,1 removal of iron from low iron containing minerals,2 the development of suitable processes for the chemical cleaning and decontamination of steel surfaces,3.4 availability and transformation of iron in soils, water and sediments.5 Among several mineral acids used for the dissolution of hematite,6-S HCI is found to be most effective due to relatively higher romplexing Experimental Procedure Naturally occurring iron oxide powder collected from Barsua Iron Ore Mines, Sundargarh, Orissa, were sieved to different size fractions: -150 + 751A.,-75 + 451A.and -45 + 371A.. Mineralogical studies employing X-ray diffraction revealed that the samples contained mainly a-Fe203 with traces of magnetite (Fe304) as the iron bearing phases besides quartz (a-SiO2). The weight per cent of major elements in -150 + 751A.,-75 + 451A.and -45 + 371A.samples are: Fe(II), 66.5, ability of CI- with Fe3+ and solubility of FeCl3 compared to other ferric salts. The dissolution process is, however, greatly enhanced by the presence of reductant and/or complexing agents4.9-14. For example, the dissolution of hematite in HCI or H2SO4 in presence of various redox couples (e.g. V(III)-V(IV), 1-12, Br-Br2' Ce(III)-Ce(IV), Fe(II)-Fe(III) etc.) and complexing agents (e.g. ED TA, crphenanthroline, 2,2'-Bipyridine, NTA etc.) has been found to increase than that in absence of such redox couples or complexing agents. Although a considerable amount of studies have been carried out on the dissolution of hematite in the presence and absence of reductants, no report on dissolution using both organic and inorganic reductants and their comparison is available in literature. In the present work, the dissolution of naturally occurring hematite in HCI medium in presence of several organic and inorganic reductants in order to find the most effective reductant for the dissolution process has been reported. The promoting effect of various reductants and its probable reasons are also discussed. 68.0 and 69.5; Fe(III), 0.18, 0.35 and 0.92; SiO2, 4.43, 2.80 and 0.66 and Al2O3' 0.09, 0.07 and 0.01, respectively. Most of the experiments were performed with samples having size fraction -75 + 451A.. All the reagentsused were of AR grade. Dissolution experiments were carried out in a three necked 500 mL capacity flat bottom reaction vessel containing 200 mL of hydrochloric acid of desired concentration. A reflux condenser and a thermometer port were fitted in its two openings while the third opening was used for charging samples and withdrawing leach liquor. The reactor was magnetically. stirred and heated with a heating mantle. A critical speed (500 rpm) was maintained to prevent diffusion of reactants in the bulk solution from being the rate limiting. When the desired temperature is reached, 20g of sieved hematite with or without reductants were introduced into the reactor. At pre-determined time intervals, 2 mL of aliquot was withdrawn for estimation of Fe2+, F~olal and free acid content using standard methodsl5. At the end of the dissolution experiment, the undissolved mass was fil- r I 244 INDIANJ. ENG.MATERSCI.,DECEMBER1996 100 100 80 :'" . 80 "' ~ c .0 c' 0 :;- := 60 60 0 ~ III -III 0 .- = "0 . .N. :0 4 40 ~ "" 14 20 14 14 14 2 0 , 0 0 0 1 2 3.' 5 6 1 2 [Free ] Qcid),M 4 Fig. 2-Correlation of free acid concentration with dissolution of hematite at different time intervals (Liquid/solid = 10:1, 7 Tlm~,h T= 106°C) Fig. I-Dissolution of hematitein HCI asa functionof time. (Liquid/solid= 10:1,T = 106°C) g HCI (~ 200 mL 1.97 M HCI) only 5.51:>g hem- tered, washed thoroughly, dried at 120°C and finally subjected to chemical analyses for mass balance and XRD study for identification of mineral phases. XRD patterns of the residue showed characteristic Peaks of Fe o and Fe o of re2 3 3 4 duced intensities and prominent peaks for a-SiO2. The effect of different variables, viz., acid concentration, temperature, particle size and liquid/solid ratio, reductant concentration and time of reaction were also studied. Results and Discussion Effect of acid concentration-The effect of [HCI] (1.97-7.88 M) on dissolution of hematite was studied keeping the temperature, liquid/solid ratio and particle size constant (Fig. 1). As expected, the percentage of dissolution increases .., [HCI]. Approximately parabolic-type increase . f with m the % of dissolution as well as formation 0 ~~/ r~ n) ' m th I e h eac li quor . th Wi t respec t o. [HCI] atite comes into solution after 8 h against the expect~d 1?7~ hematite. This indicates .~at the reactio? is Virtually stopped when the acid ~o~centration .becomes 0.9M (= 6.56 goHC!). Thi~ is further evident. from. the. plots of Yo dissolution versus free acid which mtersect at a common . pomt (F.ig. 2 ). Effect of temperature-To study the effect of temperature, experiments were carried out in the temperature range 70-106°C keeping all other conditions constant. Fig. 3 shows that the dissolution of hematite increased almost linearly at low temperatures and becomes assymptotic at higher temperatures. This is due to higher initial rate of dissolution at higher temperatures. Under identical conditions, the formation Fe(n) increases with increase in temperature, which may also attribute to the higher rate of dissolution. E~ect 0if part lcI e Slze- The fracti on 0f iron ' ex, .., . tracted versus time . plots i ,., , . for different ., pamcle , SiZe . were observed from the plots. This increase of fractions at ~ed tempe,ratu~e, liquid/solid ratio d I ti' . th .' [HCI] .. b d t and [HCI] are illustrated m Fig. 4. It shows that as iSSO u on Wi mcrease m is ascn eo. ... the increase in [CI-] and also [H+P6. Besides this ~e pamcl~ s~e ~ecrease~ the ~ate of dissol~ti~n an increase in the formation of Fe2+ in leach li- mcreas~s, mdicating ~e dissolution of hema~te m quor with increase in acid concentration is an HCI ffilght be. cheffilcally. contro~ed. Th~ higher added factor for higher dissolutionl. ~e(n) content m sm~er SiZe fraction and m leach The main reaction taking place during hematite li9uor ~y also attnbute to the enhanced rate of dissolution in HCI is given by Eq. (1): dissolution. Fe2O3 + 6HCI = 2FeCl3 + 3H20 ...(1) Effect of liquid/solid ratio-The effect of liquid/ A simple calculation using Eq. (1) shows that 20 g solid ratio (mUg) on dissolution of hematite was iron ore (= 19.44 g hematit~, Fe203) requires studied keeping other parameters constant (Fig. 26.7 g HCI for complete dissolution as FeCI3. 5). As expected, the rate of dissolution increases However, experimentally it is found that in ~4.36 as the liquid/solid ratio changes from 5:1 to 20:1. . , .. I PARmA& DAS:REDUcnVEDISSOLUTION OF HEMATITE 245 100 100 8 ~ ..~ ~ c 0 80 c 0 -" 6 - .-0 -WI " 60 WI "0 :0 WI WI :0 '0 .0 ~ . 5.1 661 A .40. ~ ..20: 10: 1 1 2 20 0 5 Liquid/solid 8 1m_, 90 3 R_ductants 1 So4ium lulp'ito Z Zi.. J O.ali. a.id ~ 80 8 . .~ C 0 9 Sta..ou. a.id .h'orido 10 Forroul .hlorido , Hydroqui.ono ~ C .-0 ..60 :. Particl. 0 ."; size - WI 0 .~ 40 III .~ 10 1 -150,41 .. '0 .L&o 7 Hydro'7Iami.. hydro.hlarldo 8 Hydra.i.o , Glu.o.o S A..orbi. ~ mL,9 Fig. 5-Effect of.liquid/solidratio on dissolutionof hematite. ([HCl]= 5.90M,T = 106 .C) Fig. 3-Dissolutionof hematiteat differenttemperature as a functionof time(Liquid/solid= 10:1,[HCl] = 5.90M) 100 fatlo, 2 -15,41 'a 3 -451J L.. 20 0 60 0 3 Time.h ' Fig. 4-Effect of particlesizeon dissolutionof hematiteas a functionof time(Liquid/solid= 10:1,[HCl] = 5.90M, T=106.C) Effect ." of reducing agents-The dissolutIon of hematite in presence of varying amount of reductants (0,.5 wt.%) studied at fixed temperature, liquid/solid ratio and [HCl] are illustrated in Fig. 6. It is interesting to note that, with increase in reducing agents from 0 to 2%, the dissolution increases sharply except in the case of sodium sulphite where a marginal increase is found even at 5%. However, further increase in reductant con.centrations (upto 5%) do not show an appreciable increase in dissolution except in cases of SnCI2, FeCI2,oxalic acid and glucose. The representative time plots for dissolution of hematite in presence of reductants are given in 500 2 3 [R.ductantJ,% 5 Fig. 6-Dissolution 01 hematite as function of reductant concentration ([HCl] = 5.90M, T'= 106 .C) Fig. 7. Similar plots were also obtained in the cases of other reductants. For better comparison, the reductants are divided. into three categories based on their electrochemical reactions: (i) reductants which consume H+ with release of electrons, viz., Zn, Na2S03, (ii) reductants which release H+ along with electrons, viz., ascorbic acid, glucose, hydro-quinone, oxalic acid, hydroxylamine hydrochloride and hydrazine and (ill) reductants which releas~ H + ions and electrons consuming Cl- ion. 246 INDIANJ. ENG.MATERSCI.,DECEMBER1996 Table 1-Fe(II) formationafterfour hoursof dissolution andits comparison withexpected values[Hematite(-75 + 45 14)= 20g,[reductant]= 2%{w/w),[HCl] = 5.9 M (200 mL)andtemperature= 106.C] Sl. Reductants No. Electron released/ [Reductants],M Fe(II)expected',g MaximumFe(II) expected", g Fe(II)found,g . molecule 1 2 3 4 5 6 7 8 Nil SodiumSulphite 2, 0.158 Zinc 2 0.0305 Oxalicacid 2 0.0159 Glucose 2 0.0111 Ascorbicacid 2 0.0113 Hydroquinone 2, 0.0180 Hydroxylamine 2 0.0287 hydrochloride 9 Hydrazine 4 0.0154 10 Tinchloride 2 0.0169 11 Ferrouschloride 1 0.0158 *Fe(II)calculated basedonelectrochemical reactionof reductants **Sumof Fe(II)expected 1and Fe(II)formedwithoutreductant (0.042g) 10 80 .SnCl2 ;c ~ 60 ~ "' :0 .." LL 1 2 3 4 5 Nil Oxalicacid Hydroxylamine hydrochlorid. SnCI2 F.CI2 2 0.3529 0.6814 0.3545 0.2479 0.2524 0.4021 0.6411 0.3949 0.7233 0.3965 0.2899 0.2944 0.4441 0.6831 0.042 0.0479 0.0804 0.2404 0.2665 0.2856 0.3613 0.3782 0.6862 0.3764 -0.4420 0.7282 0.4184 0.4310 0.4280 0.4550 RCHO -+ RCOOH + 2e ...(6) C6H6O2 -+ C6H4O2 + 2H+ + 2e ...(7) N2Hs+ -+ N2 + 5H+ + 4e ...(8) 2NH3OH+ -+ H2N2O2 + 6H+ + 4e ...(9) + 2HCl -+ SnCl4 + 2H+ + 2e ...(10) (whereR = CSHIIOS) In case of glucose, oxidation of aldehyoe group to the acidic group has been considered whereas th lib d SO f d 1 hi .. e erate 2 rom so IUm SUp te IS OXIdisedtoSO~- in presence of Fe3+(ref. 17). .. Table 1 presents the concentration of vanous reductants used; expected Fe2+ comes into solution based on the electrochemical reactions and Fe2+ actually found after 4 h of dissolution. A 1 . 2 Time,h Fig. 7-Dissolutionof hematitein presence of reductants asa functio~Qftime ([HCl] = 5.90~. [reductant!= 2 wt. % T= 106 C) much lower value of Fe2+ formation in the case of Na2S03 is probably due to the incomplete utilisation of evolved S02' In case of zinc, because of its high electropositive nature, conversion to Zn2+ is completed before any appreciable amount of Fe203 dissolution takes place. In the second category (SI Nos 4-9) the formation of Fe2+ is also The presence of reducing agents during dissolution reduce a part of FeCI3 to FeCI2. The extent of reduction is a complicated process w-rnch is a function of several factors such as concentration and nature of reductants, reduction potentials and reaction medium. So it is worthwhile to present ~he °.xidation reactions ~f variou~ reductan~s us~d III this study. The reactions taking place III acId medium are as follows: Na2S03 + HCl -+ S02 + H2O + 2NaCI ...(2) S02 + 2H2O -+ SO~- + 4H+ + 2e ...(3) Zn + 2HCl -+ ZnCI2 + H2 + 2e ...(4) H2C2O4 -+ 2H+ + 2C02 + 2e ...(5) lower, but comparable with expected values indicating incomplete reaction of the reductants under the expelimental conditions. The high values of Fe2+ in case of hydroxylamine hydrochloride is, perhaps, due to its high concentration whereas in case of hydrazine sulphate, the same is due to more" number of electrons released per molecule. In case of t?e third category, (Sl Nos :0 & 11), Fe2t formation are remakably same WIth that of expected values. In order to understand the importance of Fe2+ formation during dissolution, Fe3+IFe2+ ratios at different time intervals are calculated and compared with that of Fe203 dis'solution. 0 0 "- '" J . , PARIDA & DAS: REDUCI1VE DISSOumON OF HEMATI'I'E 247 Table 2-Relationshlp betweenFe3+IFe2+ratio with hematitedissolutionat different time intervals [Hematite( -75 + 4.5 It) = 20g,[Reductant]= 2% (w/w), [HCl] = 5.9 M (200 nIL) and temperature= 106 .C] S No. Ih Reductant 1 2 3 4 5 6 7 8 4h Fe3+/Fe2+ Fe dissolution,% Fe3+/Fe2+ Fe dissolution,% Fe3+/Fe2+ Fe dissolution,% Nil SodiumSulphite Zinc Oxalic acid Glucose Ascorbic AcidHydroquinone Hydroxylamine hydrochloride Hydrazine Tin chloride Ferrouschloride 9 10 11 2h 223 191 122 59 49 40 32 27 57.5 58.5 60.4 63.5 64.6 71.8 71.5 72.2 228 209 142 88 51 .42 34 30 70.7 74.0 76.1 79.5 81.7 83.4 84.5 85.3 .278 251 151 51 46 43 33 33 86.1 89.0 90.1 91.3 91.7 91.9 94.0 94.3 24 23 22 72.7 72.9 73.3 26 27 25 85.3 85.6 86.3 29 29 27 95.0 95.5 96.5 Table 2 presents Fe3+IFe2 + ra~,o,s in the leach ence to the extent <;>f2 w.t, 9/0 reduce the dissolu- liquor found after 1,2 and 4 h"of dissolution tion (> 90°/9 of Fe203) time from 6 to 3h, along with the percentage Fe2O3 dissolution, It is f thi blth th d ' I '. Ac know Iedgemen ts seen rom s ta e at e 1SS0ut10n Increases Th eau thors are thankfu I t 0 Pr0f , H S Ray, D1'Simil ' b th d ' r 3+ /r= 2+ ' W1 ecrease In re / J.'e rattos, ar 0 serv. h al b d b Chi ,. d H rector, Regional Research Laboratory, Bhubanes, .4 d D S BR H din ' Ch ' als ations ave so een ma e y anzm an orTh 0/ fth d d .war, an r ao, ea, organic effilc D '" 1V1S10n to r encouragemen t an d In ' t eres t In ' thi s Wltz , e wt /0 0 .. e re uctants are expresse ( In . terms Table of co?centration for better coml?anson 1). Since the molar concentrations see of the reductants are not the same in all cases, comparison of their effec~veness cannot be done t~ing all of them at a time, However, among sodiUm sulphite, oxalic acid, tin chloride and ferrous chloride, where the concentration of promoter, are almost same (- 0,015 M), their effectiveness follow d 1:- CI S CI > ali .d > sod rum .lear an or er re 2 n 2 ox c aC1 sulphite. Similarly, among zinc, hydroxylamine hy- - drochloride"' and hydrazine sulphate where the concentration is almost equal to 0,03 M, the order of effectiveness is: hydrazine sulphate -hyd I . h d hl 'd > ' roxy amme y roc on e ZinC, Conclusions Th d . I . f h " HC I .I' e 1SS0ution. 0 .ematite 1? 1Sa comp 1cated process which 1S a function of several factors such as acid concentration, temperature, particle size and liquid/solid ratio, It increases wi$ increase in free acid and Fe2 + concentration in . f th ~eleac,h liquor, In ~e I?resence 0 reductant e d1ssolution of hematite 1S greatly enhanced, The priniary function of the reducing agents is to reduce a part of Fe3+ to Fe2+ and thereby lowers Fe3+ IFe2+ ratio, Reductants to the extent of 1 to d th d ' I ti. t ' 5 to/ f h t 't W ,/0 0 ema 1 e re uce, e 1SS0 u on lffie ap- prec1ably from that of WlthOUt reductants, FeCI2 and SnCI2 are found to be the best and their pres- work' ' References 1 Kanungo S B & Jena P K, Hydrometallurgy,21 (1988) 41. 2 Patermarakis G & Paspaliaris Y, HydrQmetallurgy,23 (1989)77. " , 3 Blesa M,~. & Marot.oA J G, ill Dec,ontamlnatlon of NucFacuttles, (AmencanNuclear Society),1983,1. 4 Chiarizia R & Horwitz E P Hydrometallurgy27 (1991) 339. ' , 5 Zinder B, Furrer G & Stumm W, Geochim Cosmochim Acta,50 (1986)1861. . 6 Azuma K & KametanlH; Trans Metall Soc A1ME, 230 (1964)853. 7 Surama'V S & Warren H I, Trans lnst Min Met, 78 (1969)133. 8 Warren H I & Roach G I D, Trans lnst Min Met, 8 (1971)152. 9 ValverdaN, Ber Bunsenges PhY$Chern,80 (1976)333. 10 Gorichev I G, Kipriyanov N A, Zh PriklKhim (Leningrad),52 (1979)508. 11 LeeJI&Kn°:-vnLM,Hydrometallurgy,27(1983) 194. 12 Lu Z-Y & Muir D M, Hydrometallurgy, 21 (1988)9. 13 Afonso M D S, Morando P J, Blesa M A, Banwart S & StummW,JColloidlnteifaceSci,138(1990)74. 14 Majirna H, Awakura Y & Mishirna T, Met Trans, 16B (1985)23, 15 Vogel A I, A text book of quantitative analysis,3rd ed, Longman,(1969),309. , 16 Warren (1987) G 57. M, Kill S -H & Hemen H, Met Trans, 18B 17 Tiwari B L, Kolbe J & Hayden H W (Jr), Met Trans,lOB (1979)607.