SU833549A1 - Method of purifying sulfuric acid solutions from arsenic - Google Patents
Method of purifying sulfuric acid solutions from arsenic Download PDFInfo
- Publication number
- SU833549A1 SU833549A1 SU782677909A SU2677909A SU833549A1 SU 833549 A1 SU833549 A1 SU 833549A1 SU 782677909 A SU782677909 A SU 782677909A SU 2677909 A SU2677909 A SU 2677909A SU 833549 A1 SU833549 A1 SU 833549A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- weight
- mouse
- purification
- parts
- solution
- Prior art date
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
(54) СПОСОБ ОЧИСТКИ CEPHOKHCJbK РАСТВОРОВ(54) CEPHOKHCJbK SOLUTION CLEANING METHOD
ОТ мдаь кА Предпочтительно сульфид щелочного металла вводить в количестве 5-10 вес.ч. на 1 вес.ч. мышь ка, а хлорид бари или кальци в количестве 0,07-0,36 вес.ч. на 1 вес.ч. 50 , Пример. Очищаемый раствор имитирующий раствор, образующийс при мокрой очистке мышь ксодержащих газов олов нной плавки, и содержащий 1.6г/л мышь ка; 91,5 мг/л железа; 8.7г/л цинка; 81 г/л сульфатов ( в пересчете на S0) при рН 0,5.о6рабатывают сульфидом натри и хлоРИДОМ кальци . Полученные результаты обработки приведены в табл.1. Т а. б л и ц а 1FROM MDA KA Preferably, an alkali metal sulphide is introduced in an amount of 5-10 parts by weight. on 1 weight. mouse, and barium chloride or calcium in the amount of 0.07–0.36 parts by weight. on 1 weight. 50, Example. The solution to be purified is a simulating solution formed during the wet cleaning of mice with tin-smelting gases containing gaseous mice and containing 1.6 g / l of mouse; 91.5 mg / l of iron; 8.7g / l zinc; 81 g / l of sulphate (in terms of S0) at pH 0.5 oo is treated with sodium sulphide and calcium chloride. The results of processing are given in table.1. T a b l and c a 1
Из приведенных данных видно,что При осаждении мышь ка сульфидом натри без -добавки хлористого кальци (опыты 1, 3, 6 и 8) концентраци мышь ка в растворе снижаетс до 3,5-2,0 мг/л при соотношении .5 : As 5-10:1. Дальнейшее увеличение дозы сульфида щелочного металла не приводит к углублению степени очистки.Введение совместно с NajS хлорида кашьци в количестве 0,07 вес.ч. на 1 вес.ч. иThe data show that during precipitation of the mouse with sodium sulfide without the addition of calcium chloride (experiments 1, 3, 6 and 8), the concentration of the mouse in the solution decreases to 3.5-2.0 mg / l with a ratio of .5: As 5-10: 1. A further increase in the alkali metal sulphide dose does not lead to a deepening of the degree of purification. The administration together with NajS kashtsi chloride in an amount of 0.07 wt.h. on 1 weight. and
1 2 31 2 3
I , выше (опыты 5, 7 и 9) приводит кI, above (experiments 5, 7 and 9) leads to
снижению концентрации мышь ка в растQ воре до 0,0-0,5 мг/л. Увеличениеa decrease in the concentration of the mouse in rastQ thief to 0.0-0.5 mg / l. Increase
дозы хлорида кальци выше 0,36 вес.ч. на 1 вес.ч. S0j приводит к росту объема выдел ющегос осадка, а потому нецелесообразно.doses of calcium chloride above 0.36 weight parts. on 1 weight. S0j leads to an increase in the volume of precipitates deposited, and therefore impractical.
Пример 2. Тот же раствор, что и в примере 1 oбpaбaтывa oi сульфидом натри и хлоридом бари . Результаты обработки приведены в табл. 2. Example 2. The same solution as in Example 1 was treated with sodium sulfide and barium chloride oi. The results of processing are given in table. 2
. .Таблица2. .Table 2
3,50 3.50
Claims (3)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU782677909A SU833549A1 (en) | 1978-10-26 | 1978-10-26 | Method of purifying sulfuric acid solutions from arsenic |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU782677909A SU833549A1 (en) | 1978-10-26 | 1978-10-26 | Method of purifying sulfuric acid solutions from arsenic |
Publications (1)
Publication Number | Publication Date |
---|---|
SU833549A1 true SU833549A1 (en) | 1981-05-30 |
Family
ID=20790867
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU782677909A SU833549A1 (en) | 1978-10-26 | 1978-10-26 | Method of purifying sulfuric acid solutions from arsenic |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU833549A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0166469A2 (en) * | 1984-05-16 | 1986-01-02 | Metallgesellschaft Ag | Method for removing arsenic from waste sulphuric acid |
DE4015489A1 (en) * | 1990-05-14 | 1991-11-21 | Aquamot Ag | Freeing waste material from heavy metals and dioxin(s) - by treating aq. slurry with active gas mixt. and precipitating heavy metals |
-
1978
- 1978-10-26 SU SU782677909A patent/SU833549A1/en active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0166469A2 (en) * | 1984-05-16 | 1986-01-02 | Metallgesellschaft Ag | Method for removing arsenic from waste sulphuric acid |
DE4015489A1 (en) * | 1990-05-14 | 1991-11-21 | Aquamot Ag | Freeing waste material from heavy metals and dioxin(s) - by treating aq. slurry with active gas mixt. and precipitating heavy metals |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US3778368A (en) | Disposal of metal-containing waste water | |
GB1484819A (en) | Process for removing chloride ions from an aqueous solution of zinc sulphate | |
EP0709475A1 (en) | Procedure to obtain mercury metal from products containing mercuric chloride | |
SU833549A1 (en) | Method of purifying sulfuric acid solutions from arsenic | |
GB1478345A (en) | Process for purifying water containing suspended matter | |
ES471032A1 (en) | Purification process | |
KR100300815B1 (en) | Method for obtaining mercury metal from product containing mercury chloride | |
FR2544750B1 (en) | PROCESS FOR TREATING A PURGE SOLUTION, IN PARTICULAR FOR AN ELECTROLYTIC ZINC EXTRACTION PROCESS | |
GB1524552A (en) | Process and apparatus for the purification of wetprocessed phosphoric acid | |
FR2416955A1 (en) | NON-POLLUTING TREATMENT OF URANIFIC ALKALINE EFFLUENTS CONTAINING SO4 IONS = | |
GB2004469A (en) | Sulphuric acid concentration | |
SU496237A1 (en) | The method of purification of zinc sulphate solutions from chlorine | |
FR2416954A1 (en) | NON-POLLUTING TREATMENT OF URANIUM EFFLUENTS FROM AN ALKALINE ATTACK OF A URANIUM ORE CONTAINING SULFUR | |
SU380587A1 (en) | METHOD FOR DECOMPOSITION OF CHLORIDE BARRY PRODUCTION SLUDGE | |
SU148035A1 (en) | The method of producing ammonium sulfate | |
SU973484A1 (en) | Process for producing magnetite and calcium sulfate from waste pickling liquors containing iron sulfate | |
SU1261916A1 (en) | Method of treating flushing water sediment | |
JPS63296890A (en) | Treatment of waste water | |
SU899493A1 (en) | Process for purifying sulphat-containing effluents | |
SU808372A1 (en) | Method of acid waste water purification | |
FR2372119A1 (en) | PROCESS FOR TREATMENT OF BRINE CONTAINING MAGNESIUM CHLORIDE | |
SU710985A1 (en) | Method of waste water purification from arsenic | |
SU1740320A1 (en) | Method of preparing ferrum oxide | |
SU833556A1 (en) | Method of purifying aqueous solutions from metals | |
SU126481A1 (en) | Method for producing cobalt oxides |