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Polish Journal of Chemical Technology, 13, 4, 53 — 56,Pol. 2011, J. Chem. 10.2478/v10026-011-0049-y Tech., Vol. 13, No. 4, 2011 53 Utilization of the post – fi ltration lye from the soda-chlorine-saltpetre method of soda production Sebastian Drużyński*, Mieczysław Trypuć, Urszula Kiełkowska, Krzysztof Mazurek Nicolaus Copernicus University, Faculty of Chemistry, Department of Chemical Technology, Gagarina 7, 87-100 Toruń, Poland * Corresponding author: e-mail: [email protected] The optimal conditions were determined for the precipitation of ammonium metavanadate from the solutions of ammonium nitrate with the use of sodium metavanadate. The experiments were performed with the molar ratio of salts NH4NO3:NaVO3 1.5:1 at temperatures 293, 303, 313 and 323 K. Based on the obtained results, the optimal time of the process was determined as 5 h at 293–303K. Under these conditions, the achieved yield of the precipitation process was ~98.7%, while the contents of the vana- dium salts in the post – fi ltration solution was ~0.02%. Keywords: SCS method, double exchange, ammonium nitrate and ammonium metavanadate. INTRODUCTION EXPERIMENTAL PART Production of sodium carbonate with the Soda-Chlo- rine-Saltpetre method (SCS) gives valuable by-products Method – chlorine and solution of ammonium-sodium saltpetre Experiments were conducted at 293, 303, 313 and 323 composed of 80% NH4NO3; 18% NaNO3 and 2% NaCl K to determine the infl uence of the addition of sodium as recalculated to solids1. That solution is a material for nitrate on the reaction yield. The time dependence of the production of nitrogenous fertilizer. The authors of the yields ( ) of precipitation relative to ammonium the SCS method had assumed processing of that liquor ions were calculated according to equation (2) where by evaporation and crystallization of ammonium-sodium the excess of the used ammonium nitrate relative to the saltpetre. That way is diffi cult due to a possibility of the amount of sodium metavanadate was accounted. uncontrolled decomposition of ammonium nitrate which is catalyzed by the chloride ions remaining in the solu- tion of sodium nitrate after oxidation of sodium chloride (2) with the nitric acid1–3. where: – initial concentration of ammonium ions The aim of the research is to eliminate the danger oc- in the solution, curring during the recovery of solid ammonium-sodium – concentration of ammonium ions after time (t). nitrate by the evaporation of the post – fi ltration solution in the process of soda production with the SCS method, – excess of ammonium ions (0,830M). as well as to improve the material and economical ef- At each temperature, the measurements were performed fi ciency of that method. The research on partial utiliza- twice. Ammonium metavanadate was precipitated from the tion of the post – fi ltration lye from the classic Solvay solutions of 2.5 M ammonium nitrate with and without 1.0 method, indicates the possibility of the use of sodium M sodium nitrate. At all temperatures, the molar ratio 1.5:1 metavanadate instead of calcium hydroxide suspension4,5. of salts NH4NO3:NaVO3 was maintained. That approach to the utilization of the post – fi ltration Based on the preliminary research on the precipitation lye from the SCS method is based on a reaction of of ammonium metavanadate from the ammonium nitrate sodium metavanadate with ammonium nitrate, present solutions, the maximum initial concentration of 2.5 M for in the solution, according to equation (1). NH4NO3 was determined to give the optimal conditions for stirring and the high yield of reaction. For the solutions of NH NO + NaVO ↔ NH VO ↓ + NaNO (1) 4 3 3 4 3 3 higher initial concentration of ammonium nitrate, the reaction From the research performed on the mutual solubility of mixture was solidifi ed during the dosage of the reagent into salts for the pairs of exchanging salts NH NO + NaVO 4 3 3 the required amount of solid sodium metavanadate, which + NaNO + NH VO + H O and four ternary subsystems: 3 4 3 2 made the monitoring of the reaction progress impossible. NaVO + NaNO + H O, NH VO + NH NO + H O, 3 3 2 4 3 4 3 2 Ammonium metavanadate was precipitated from the NaNO + NH NO + H O, NH VO + NaVO + H O it 3 4 3 2 4 3 3 2 ammonium nitrate solutions in the 200 cm3 Erlenmeyer follows that the highest yield of the conversion reaction is fl ask with the grinded neck. The required amount of achieved for the composition of the solution corresponding sodium metavanadate was weighted and then 100 cm3 to the ternary invariant point P . The solution at this 1 6,7 of the appropriate ammonium nitrate solution was dosed point remains in the equilibrium with three salts in the solid with the one – mark pipette. The fl ask was corked and phase: NaNO , NH VO and NaVO . During the precipita- 3 4 3 3 thermostated in the water bath with the constant stirring. tion process, the situation in which the mixture of crystals During that process, the samples of the clear solutions is obtained instead of the pure product (NH VO ) should 4 3 were collected for determination of changes in the solu- be avoided. Therefore, there is a necessity to determine tion density, as well as concentration of ammonium and the physico – chemical parameters such as time, molar vanadate ions. Samples were collected in the appropriate ratio of reagents and the initial concentration of the brine time intervals: every 1 hour during fi rst 5 hours, then of ammonium and sodium nitrates, which cause that the every 24 hours until reaching the equilibrium. pure product will be obtained with the possibly high yield. 54 Pol. J. Chem. Tech., Vol. 13, No. 4, 2011 ANALYTICAL METHODS LABOMED with the 10 mm quartz absorption cells. The concentration of ammonium ions was determined with the Ronchese method. It is based on the reaction of RESULTS AND DISCUSSION formaldehyde with ammonium ions according to equa- Changes in ammonium and vanadate ions concentra- tion (3). In that reaction the nitric acid is formed in an tions, densities and the dependence of yields of the amount equivalent to the amount of ammonium ions 8. conversion reaction on time and the conditions of the 4NH4NO3 + 6HCHO → (CH2)6N4 + 4HNO3 + 6H2O ammonium metavanadate precipitation are presented (3) in table 1. To determine the concentration of vanadate ions, After the fi rst hour of the conversion process, the the spectrophotometric method was used with 4–(2– achieved yield is approximately 80% in both cases with pyridylazo) resorcinol (PAR). Vanadate ions form a and without sodium nitrate (table 1). The excess of am- red – purple complex ion with PAR. That compound monium nitrate relative to sodium metavanadate and the has a maximum absorption at 540 nm, and the molar increase of temperature does not signifi cantly affect the absorption coeffi cient is 3,6.104 dm3.mol-1.cm-1 9–11. The time the equilibrium is reached. In both cases, in the measurement was performed with the double – beam UV presence or absence of sodium nitrate, the equilibrium – Vis spectrophotometers Hitachi U-2000 and UVD–3000 was reached after ca. 20 h. Table 1. Effect of time and temperature of precipitation on the fi eld of ammonium metavanadate and composition of the post – fi ltration lye Pol. J. Chem. Tech., Vol. 13, No. 4, 2011 55 In the excess of ammonium nitrate relative to sodium the fi nal product sodium nitrate, for the molar ratio metavanadate, it can be concluded that the negative ef- ammonium nitrate to sodium metavanadate of 1.5:1 as fect of sodium nitrate on the equilibrium is fully elimi- found after 5 h of thermostating. nated. In all investigated cases, the complete conversion It has to be stated, that at selected temperatures, the of sodium metavanadate was achieved. The additional lowering of the reaction yield for the solutions with advantage is the signifi cant limitation of concentration sodium nitrate is insignifi cant relative to that for the of vanadate ions caused by the salting out effect of stoichiometric amounts of reagents. This indicates that ammonium nitrate on ammonium metavanadate. This the used excess of ammonium nitrate effi ciently com- limits the production loses of the vanadium compounds. pensates the negative effect of sodium nitrate on the Analysis of the experimental data (Table 1) indicates process yield. Also, Figure 1 reveals that the increase of that the state close to the equilibrium is reached already temperature negatively affects the yield of the conversion after 5 hours of reaction. Continuation of the process reaction, and the effect is more signifi cant for solutions longer than 5 h, and the simultaneous decrease in the containing sodium nitrate. concentration of ammonium ion in the solution, does not The signifi cant aspect of the research is the determi- signifi cantly increase the yield of reaction. It should be nation of the conditions at which the obtained product emphasized that the extension of the time of conversion reveals the minimal contamination with the vanadium results in the continuous increase of the vanadate ion salts. Contamination of the produced sodium saltpetre concentration, thus increasing loses of vanadium com- with the vanadium compounds determines its useful- pounds. Therefore, the optimal time of the process of ness as a fertilizer or is related to the process loses of ammonium metavanadate precipitation should be 4 – 5 h. the vanadium compounds. Figure 2 presents the effect Figures 1 and 2 present the calculated yields of reac- of temperature and the presence of sodium nitrate on tion and the contents of the vanadium compounds in the amount of vanadium salts contaminants in sodium nitrate – the solid product after 5 h of process conduct- ing.

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