Abstract

Technology used to produce high purity anhydrous rubidium perrhenate on an industrial scale from high purity perrhenic acid and rubidium nitrate by the ion-exchange method is described in this paper. This material is dedicated to catalyst preparation, therefore, strict purity requirements have to be fulfilled. These are satisfied by combining rubidium ion sorption on an ion exchange column and the subsequent elution of the high purity perrhenic acid solution, followed by crystallization, evaporation, purification, and drying. In the current study, rubidium and rhenium contents were found to be 22.5 wt.% and 55.4 wt.%, respectively, while contaminations were as follows: <2 ppm As, <2 ppm Bi, <5 ppm Ca, <5 ppm Cu, <3 ppm Fe, <10 ppm K, <3 ppm Mg, <5 ppm Mo, <2 ppm Na, <5 ppm Pb, and <3 ppm Zn.

Highlights

  • Preparation methods of rubidium perrhenate are poorly described in scientific databases.In particular, there is no information on the industrial scale production of this compound

  • Preparation is generally based on the neutralization of perrhenic acid solution by rubidium carbonate or hydroxide in equimolar amounts, resulting in the precipitation of rubidium perrhenate [4,5]

  • The post-washing solutions from elution were divided into two parts—the first was combined with the solution subjected to concentration, while the other, was mixed with mother liquors and post-purification solutions and sent for rubidium perrhenate preparation (>40 nm)

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Summary

Introduction

Preparation methods of rubidium perrhenate are poorly described in scientific databases. Perrhenate, chromium(III) perrhenate, and cesium perrhenate production and has been described in past works [8,9,10,11] This method (for nickel(II) and cobalt(II)) has been implemented in industry practice. The obtained high-purity materials may be used for the production of inorganic and organic Re compounds, like catalysts, e.g., methyltrioxorhenium (MTO), rhenium carbonyl (Re2 (CO)10 ), and its derivatives [12,13]. It may be an important additive to heterogeneous (e.g., Al2 O3 - or SiO2 -based) catalysts [14,15,16,17]. Unnecessary components, like nitrate and ammonium ions, are eliminated

Materials
Preparation of Rubidium Perrhenate by Ion Exchange
Static Condition
Dynamic Test
Crystalization and Purification Test
Characterization
Selection of Ion-Exchange Resin—Sorption Stage
EffectPFC100 of Temperature on the Rubidium
Effect of Contact contact
Effect of the Rubidium Concentration on Rubidium Sorption Efficiency
Selection of Ion-Exchange Resin—Elution Stage
Effect of Contact Time on the Rubidium Elution Efficiency
Effect of Temperature on the Rubidium Elution Efficiency
Influence of the Rhenium-To-Rubidium Ratio on Rubidium Elution Efficiency
Analysis of Three Cycles of PFC100x10 under Dynamic Conditions
No 2 BV1 3 BV2 4
3.10. Crystallization and Purification Stages
3.11. Thermal
Drying
3.12. Developed Technology Scheme
11. Changes
Conclusions
Full Text
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