SU1535603A1 - Method of extracting ions of transition metals from aqueous solutions - Google Patents
Method of extracting ions of transition metals from aqueous solutions Download PDFInfo
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- SU1535603A1 SU1535603A1 SU874320140A SU4320140A SU1535603A1 SU 1535603 A1 SU1535603 A1 SU 1535603A1 SU 874320140 A SU874320140 A SU 874320140A SU 4320140 A SU4320140 A SU 4320140A SU 1535603 A1 SU1535603 A1 SU 1535603A1
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- SU
- USSR - Soviet Union
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- aqueous solutions
- transition metals
- binding agent
- polyacrylic acid
- extracting ions
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Изобретение относитс к извлечению переходных металлов из водных растворов и сточных вод мембранными методами. Целью изобретени вл етс повышение производительности и сокращение расходов св зывающего агента. Суть способа заключаетс в св зывании извлекаемых ионов переходных металлов в тройной полимерметаллический комплекс полиакрилова кислота - ион металла - полиэтиленимин при мол рном отношении N = [ПЭИ]/[ПАК] = 0,2 - 0,8 и последующей ультрафильтрации полученной смеси через мембрану со средним диаметром пор 500 ± 50 А°. 1 табл.This invention relates to the recovery of transition metals from aqueous solutions and wastewater using membrane methods. The aim of the invention is to increase the productivity and reduce the costs of the binding agent. The essence of the method is the binding of recoverable transition metal ions into a ternary polymer-metal complex polyacrylic acid-metal ion-polyethyleneimine at a molar ratio of N = [PEI] / [PAA] = 0.2-0.8 and subsequent ultrafiltration of the resulting mixture through a membrane average pore diameter of 500 ± 50 A °. 1 tab.
Description
Изобретение относитс к способу извлечени металлов из водных растворов и сточных вод мембранными мето-- дами и может быть использовано в цветной металлургии, гальванопластике , в химической промышленности, а. также в других отрасл х народного хоз йства дл очистки сточных вод и создани бессточных технологических схем.The invention relates to a method for extracting metals from aqueous solutions and wastewater by membrane methods and can be used in non-ferrous metallurgy, electroforming, in the chemical industry, and. also in other areas of the national household for wastewater treatment and the creation of drainless technological schemes.
Цель изобретени - сокращение расходов св зующего агента и повышение производительности ультрафильтрационных мембран.The purpose of the invention is to reduce the costs of the binding agent and increase the productivity of ultrafiltration membranes.
Поставленна цель достигаетс предлагаемым способом извлечени исков металлов г помощью полупроницаемых мембран. Ионы переходного металла , например кадми , св зывают в тройной почимор - металлический комплекс (ТПЖ) путем добавлени The goal is achieved by the proposed method of extracting metal suits by using semipermeable membranes. Transition metal ions, such as cadmium, are bonded to a ternary low energy-metal complex (TPG) by adding
в раствор, ,,ащий ионы Cdinto a solution ,, a common Cd ions
,,
выу тето-- тиа . сшетраицасокомолекул рной (М 7-106} полиакриловой кислоты (ПАК) и высокомолекул рного () полиэтилени- мина (ПЭИ) при мол рном соотношении п 0,,8 с последующей ультрафильтрацией через мембрану.you are a tetan-- tia. cross-molecular-molecular (M 7-106} polyacrylic acid (PAA) and high molecular weight () polyethylenimine (PEI) at a molar ratio of n 0, ..., 8, followed by ultrafiltration through a membrane.
ТПМК - полиакрилова кислота - Cd2 + - полиэтиленимин образуетс за счет ионного взаимодействи между карбоксильными группами ПАК и ионами Cd1 и координационного св зывани ионов с иминными группами ПЭИ.TPMK - polyacrylic acid - Cd2 + - polyethylenimine is formed due to the ionic interaction between the carboxyl groups of PAA and Cd1 ions and the coordination binding of ions with the imine groups of PEI.
П р и м е р. К 180 мл 5,55 водному раствору CdSO добавл ют 0,3 м (2,16%) раствор полиакриловой кислоты ПАК () и 0,06 м (0,26%) раствор ПЭИ (104) с расчетом, чтобы мол рное соотношение составл ло /з ПЭИ PRI me R. To 180 ml of a 5.55 CdSO aqueous solution was added a 0.3 m (2.16%) solution of polyacrylic acid PAA () and a 0.06 m (0.26%) solution of PEI (104) with the expectation that the molar ratio was / s PEI
(Л(L
сwith
спcn
соwith
СПSP
сэse
оabout
СОWITH
вы0 ,8.you 0, 8.
ПАК 0,2; 0,4; 0,6; PAK 0,2; 0.4; 0.6;
Общий объем 200 мл. После доведени рН до 960 эти растворы раздел ют через ультрафильтрационную мембрану . Полученные результаты при атм представлены в таблице.Total volume 200 ml. After adjusting the pH to 960, these solutions are separated through an ultrafiltration membrane. The results obtained at atm are presented in the table.
Емкость тройного полимерметалли- ческого комплекса (ТПМК) по переходным металлам в 3-5 раз больше емкост индивидуальных полимерных комплексо- образователей.The capacity of the ternary polymer-metal complex (TPMK) for transition metals is 3-5 times larger than the capacity of individual polymer complexing agents.
Преимуществом предлагаемого способа по сравнению с известным вл етс также использование мембран со средним диаметром пор 500 А дл ультрафильтрации при относительно низком рабочем давлении, что позвол ет достичь нар ду с высокой степенью извлечени ионов металлов существенного увеличени производительности процесса .An advantage of the proposed method in comparison with the known method is the use of membranes with an average pore diameter of 500 A for ultrafiltration at a relatively low working pressure, which makes it possible, together with a high degree of extraction of metal ions, to significantly increase the productivity of the process.
Преимуществом предлагаемого способа вл етс также возможность многократного использовани комплексооб- The advantage of the proposed method is also the possibility of multiple use of complex
5five
5five
00
разовател ПАК и ПЭИ, что достигаетс разрушением комплекса при рН меньше 2,0 и при рН больше 11,0. Это позвол ет процесс извлечени ионов металлов осуществить в замкнутом безотходном режиме.PAC and PAYLER, which is achieved by the destruction of the complex at a pH less than 2.0 and at a pH greater than 11.0. This allows the metal ion extraction process to be carried out in a closed, waste-free mode.
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Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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SU874320140A SU1535603A1 (en) | 1987-10-21 | 1987-10-21 | Method of extracting ions of transition metals from aqueous solutions |
Applications Claiming Priority (1)
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SU874320140A SU1535603A1 (en) | 1987-10-21 | 1987-10-21 | Method of extracting ions of transition metals from aqueous solutions |
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SU1535603A1 true SU1535603A1 (en) | 1990-01-15 |
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SU874320140A SU1535603A1 (en) | 1987-10-21 | 1987-10-21 | Method of extracting ions of transition metals from aqueous solutions |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997030016A1 (en) * | 1996-02-14 | 1997-08-21 | Basf Aktiengesellschaft | Method of preparing aldehydes by hydroformylation with a rhodium catalyst and recovery of the rhodium catalyst by extraction |
-
1987
- 1987-10-21 SU SU874320140A patent/SU1535603A1/en active
Non-Patent Citations (1)
Title |
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Патент Англии № 1466150, кл. В 01 D 13/00, 1977. * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1997030016A1 (en) * | 1996-02-14 | 1997-08-21 | Basf Aktiengesellschaft | Method of preparing aldehydes by hydroformylation with a rhodium catalyst and recovery of the rhodium catalyst by extraction |
US6225507B1 (en) | 1996-02-14 | 2001-05-01 | Basf Aktiengesellschaft | Method of preparing aldehydes by hydroformylation with a rhodium catalyst and recovery of the rhodium catalyst by extraction |
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