Electrodialysis concentration of sulfuric acid

An urgent task is the development of new resource-saving technologies for deep processing of wastes from the hydrometallurgical industry for the purpose of their reuse. Membrane technologies make it possible to create closed technological cycles with the reuse of recovered components in production,...

Descripción completa

Guardado en:
Detalles Bibliográficos
Autores principales: S. A. Loza, N. A. Smyshlyaev, A. N. Korzhov, N. A. Romanyuk
Formato: article
Lenguaje:EN
RU
Publicado: Uralʹskij federalʹnyj universitet imeni pervogo Prezidenta Rossii B.N. Elʹcina 2021
Materias:
Acceso en línea:https://doaj.org/article/cfd00317b410491684d8458fc45dd5e8
Etiquetas: Agregar Etiqueta
Sin Etiquetas, Sea el primero en etiquetar este registro!
id oai:doaj.org-article:cfd00317b410491684d8458fc45dd5e8
record_format dspace
spelling oai:doaj.org-article:cfd00317b410491684d8458fc45dd5e82021-12-01T05:53:11ZElectrodialysis concentration of sulfuric acid2411-141410.15826/chimtech.2021.8.1.06https://doaj.org/article/cfd00317b410491684d8458fc45dd5e82021-03-01T00:00:00Zhttps://journals.urfu.ru/index.php/chimtech/article/view/4914https://doaj.org/toc/2411-1414An urgent task is the development of new resource-saving technologies for deep processing of wastes from the hydrometallurgical industry for the purpose of their reuse. Membrane technologies make it possible to create closed technological cycles with the reuse of recovered components in production, which allows solving many environmental problems. At the Abinsk Electric Steel Works Ltd. (Russia), during the production of copper-coated steel wire, a large amount of waste containing sulfuric acid and heavy metal salts is generated. The chemical treatment of such effluents with slaked lime and alkali produces a large amount of sludge, which causes environmental problems and leads to the irreversible loss of sulfuric acid. The problem of separating acids and salts can be solved using diffusion dialysis through anion-exchange membranes, however, to return the acid to the production cycle, the purified acid must be additionally concentrated. In this work, we studied the process of electrodialysis concentration of sulfuric acid using heterogeneous ion-exchange membranes Ralex® CMHPP and Ralex® AMHPP (manufactured by MEGA a.s., Czech Republic) which have a polypropylene reinforcing mesh resistant to acids. The main parameters of the electrodialysis concentration process have been determined – the dependence of the concentration of the regenerated sulfuric acid on the concentration at the inlet to the electrodialysis cell and on the current density, as well as the energy consumption for the process. It is shown that with the help of electrodialysis concentration it is possible to obtain sulfuric acid with a concentration of up to 180 g/L, which makes it possible to return it to the production cycle.S. A. LozaN. A. SmyshlyaevA. N. KorzhovN. A. RomanyukUralʹskij federalʹnyj universitet imeni pervogo Prezidenta Rossii B.N. Elʹcina articleion exchange membranediffusion dialysiselectrodialysis concentrationsulfuric acid recoveryChemistryQD1-999ENRUChimica Techno Acta, Vol 8, Iss 1 (2021)
institution DOAJ
collection DOAJ
language EN
RU
topic ion exchange membrane
diffusion dialysis
electrodialysis concentration
sulfuric acid recovery
Chemistry
QD1-999
spellingShingle ion exchange membrane
diffusion dialysis
electrodialysis concentration
sulfuric acid recovery
Chemistry
QD1-999
S. A. Loza
N. A. Smyshlyaev
A. N. Korzhov
N. A. Romanyuk
Electrodialysis concentration of sulfuric acid
description An urgent task is the development of new resource-saving technologies for deep processing of wastes from the hydrometallurgical industry for the purpose of their reuse. Membrane technologies make it possible to create closed technological cycles with the reuse of recovered components in production, which allows solving many environmental problems. At the Abinsk Electric Steel Works Ltd. (Russia), during the production of copper-coated steel wire, a large amount of waste containing sulfuric acid and heavy metal salts is generated. The chemical treatment of such effluents with slaked lime and alkali produces a large amount of sludge, which causes environmental problems and leads to the irreversible loss of sulfuric acid. The problem of separating acids and salts can be solved using diffusion dialysis through anion-exchange membranes, however, to return the acid to the production cycle, the purified acid must be additionally concentrated. In this work, we studied the process of electrodialysis concentration of sulfuric acid using heterogeneous ion-exchange membranes Ralex® CMHPP and Ralex® AMHPP (manufactured by MEGA a.s., Czech Republic) which have a polypropylene reinforcing mesh resistant to acids. The main parameters of the electrodialysis concentration process have been determined – the dependence of the concentration of the regenerated sulfuric acid on the concentration at the inlet to the electrodialysis cell and on the current density, as well as the energy consumption for the process. It is shown that with the help of electrodialysis concentration it is possible to obtain sulfuric acid with a concentration of up to 180 g/L, which makes it possible to return it to the production cycle.
format article
author S. A. Loza
N. A. Smyshlyaev
A. N. Korzhov
N. A. Romanyuk
author_facet S. A. Loza
N. A. Smyshlyaev
A. N. Korzhov
N. A. Romanyuk
author_sort S. A. Loza
title Electrodialysis concentration of sulfuric acid
title_short Electrodialysis concentration of sulfuric acid
title_full Electrodialysis concentration of sulfuric acid
title_fullStr Electrodialysis concentration of sulfuric acid
title_full_unstemmed Electrodialysis concentration of sulfuric acid
title_sort electrodialysis concentration of sulfuric acid
publisher Uralʹskij federalʹnyj universitet imeni pervogo Prezidenta Rossii B.N. Elʹcina
publishDate 2021
url https://doaj.org/article/cfd00317b410491684d8458fc45dd5e8
work_keys_str_mv AT saloza electrodialysisconcentrationofsulfuricacid
AT nasmyshlyaev electrodialysisconcentrationofsulfuricacid
AT ankorzhov electrodialysisconcentrationofsulfuricacid
AT naromanyuk electrodialysisconcentrationofsulfuricacid
_version_ 1718405505816199168