SU697403A1 - Method of purifying spent zinc-containing nitric acid solution - Google Patents
Method of purifying spent zinc-containing nitric acid solutionInfo
- Publication number
- SU697403A1 SU697403A1 SU762405854A SU2405854A SU697403A1 SU 697403 A1 SU697403 A1 SU 697403A1 SU 762405854 A SU762405854 A SU 762405854A SU 2405854 A SU2405854 A SU 2405854A SU 697403 A1 SU697403 A1 SU 697403A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- zinc
- nitric acid
- acid solution
- solution
- containing nitric
- Prior art date
Links
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 title description 14
- 239000011701 zinc Substances 0.000 title description 14
- 229910052725 zinc Inorganic materials 0.000 title description 14
- 238000000034 method Methods 0.000 title description 9
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 title description 5
- 229910017604 nitric acid Inorganic materials 0.000 title description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 10
- 238000000746 purification Methods 0.000 description 8
- -1 nitrate ions Chemical class 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 5
- 229910002651 NO3 Inorganic materials 0.000 description 4
- 238000006386 neutralization reaction Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- UGZADUVQMDAIAO-UHFFFAOYSA-L zinc hydroxide Chemical compound [OH-].[OH-].[Zn+2] UGZADUVQMDAIAO-UHFFFAOYSA-L 0.000 description 3
- 229940007718 zinc hydroxide Drugs 0.000 description 3
- 229910021511 zinc hydroxide Inorganic materials 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- ONDPHDOFVYQSGI-UHFFFAOYSA-N zinc nitrate Chemical compound [Zn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ONDPHDOFVYQSGI-UHFFFAOYSA-N 0.000 description 2
- NCVGSSQICKMAIA-UHFFFAOYSA-N 2-heptadecyl-4,5-dihydro-1h-imidazole Chemical compound CCCCCCCCCCCCCCCCCC1=NCCN1 NCVGSSQICKMAIA-UHFFFAOYSA-N 0.000 description 1
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- PYRZPBDTPRQYKG-UHFFFAOYSA-N cyclopentene-1-carboxylic acid Chemical compound OC(=O)C1=CCCC1 PYRZPBDTPRQYKG-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229940026651 gly-oxide Drugs 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000006396 nitration reaction Methods 0.000 description 1
- IJRVLVIFMRWJRQ-UHFFFAOYSA-N nitric acid zinc Chemical compound [Zn].O[N+]([O-])=O IJRVLVIFMRWJRQ-UHFFFAOYSA-N 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- HUAUNKAZQWMVFY-UHFFFAOYSA-M sodium;oxocalcium;hydroxide Chemical compound [OH-].[Na+].[Ca]=O HUAUNKAZQWMVFY-UHFFFAOYSA-M 0.000 description 1
- 238000000859 sublimation Methods 0.000 description 1
- 230000008022 sublimation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Electrolytic Production Of Metals (AREA)
Description
II
Изобретение относитс к способу очистки отработанного цинксодержащего азотнокислого раствора и может быть использовано в полиграфической, радиотехнической и других отрасл х промышленности .The invention relates to a method for the purification of spent zinc nitrate solution and can be used in the printing, radio and other industries.
Известен способ очистки отработанного цинке о держащего раствора путем его обработки химическими реагентами, в качестве которых используют кальцинированную соду, известь и мраморную крошку. Однако данный способ не обеспечивает возврат цинксодержащего раствора дл повторного применени в технологии , вследствие образовани труднорастворимых соединений, которые вывоз т на пол захоронени ,1.A known method of purification of spent zinc on the holding solution by treating it with chemical reagents, which use soda ash, lime and marble chips. However, this method does not ensure the return of the zinc-containing solution for reuse in the technology, due to the formation of hardly soluble compounds that are exported to the disposal floor, 1.
Кроме того, известен способ очистк цинксодержашего азотнокислого раствора путем электролитического выделени примесей с возвратом цинка в производство 2., Однако в данном способе не указано отрицательное вли ние нитратионов на выход цинка по току.In addition, a method for purifying zinc-containing nitric acid solution is known by electrolytically separating impurities with the return of zinc to production 2. However, this method does not indicate the negative effect of nitration on current output of zinc.
Наиболее близким к изсбрете:п1Ю по техт1ческой сушлюсти и достигаемому результату вл 1етс способ очистки отработа1шого цинксодержашего азотнокислого раствора, включлгошнй нейтрализацию адким натром с образорлнием суспензии гидроокиси цинка, промывку суспензии цинкатного электролита водой в соотношении 1:8 и выделение цинка электролизом З.The closest to izbreta: p1yu on technical dryness and the achieved result is a method of purification of the mature zinc containing nitric acid solution, including neutralization with adherent sodium and forming a suspension of zinc hydroxide;
Недостатком известного способл вл етс то, что он не обес, достаточно полную степень очистки ципксодержашего раствора от нитрат-ионов, содержание которых равно 4,4 г/л, что превышает допуст 5мую кбпцонтрацию (0,5О г/л) и не позвол ет полл-чить выход продукта более 08%.The disadvantage of the known method is that it does not provide a sufficiently complete degree of purification of the cyto-containing solution of nitrate ions, the content of which is 4.4 g / l, which exceeds the allowable 5th cubic concentration (0.5Og / l) and does not allow To complete the product yield more than 08%.
Целью изобретени вл етс ПОВЫШР-ние степени очистктг цин ;соде|жл1цего азотнокислого раствора от глтрат-ионов и увеличение выхода готового продукта . 3в Поставленна цель дост1 гаетс тем, что Б отработанный раствор перед нейтрализацией ввод т хлористый натрий и гфом1з1вку суслензии гищюокиси цинка осуществл ют раствором хлористого натри , И р и м е р . В отработанный раствор , содержащий азотную кислоту с ко1щентрацией 76 г/л и азотнокисл1з1Й цинк 4О г/л (по цинку), добавл ют хлористый натрий в количестве 40 г/л, Получеш1ЫЙ раствор обрабатывают 15% ным раствором едкого натра до рН-9,5 и образовавшуюс Гидроокись цинка, содержащую 82 г/л ни7рат-ионов, цромы- вают раствором хлоркстотх) натри с концентрацией 40 г/л. По данным анали за содерлсание цитрат-ионов составл ет 0,21 г/л и выход roTOF3or-o продукта (цинка) составл ет 95%. Данный способ обеспечивает повышен степени очистки цинксодержащих растворов .от нитрат-ионов и снижает содержание их с концентрации 4,4 до 0,21 г/л а также обосночивает увеличение выход готового продукта с 68 до 95%. З о р м у л а и п о б р о т о и и Слюсоб очистки отработанного цинк- солор каще1Х) азотнокислого раствора, включающий нейтрализацию едкик 1гатром с образованием суспензии гидроокиси цинка, промывку суспензии, приготовление из промытой суспензии цинкатногхэ электролита и выделение цинка электролизом. Отличающийс тем, что, с целью повыщени степени очистки от нитрат-ионов и увеличени выхода готового продукта, в отработанный раствор неред нейтрализацией ввод т хлористый натрий и промывку осуществл ют раствором хлористого натри . Источники информации, прин т1 1е во внимание при экспертизе 1. Дев тов Н. И. и др. К вопросу очистки цинкографских стоков. Полиграфи , 1975, № 7, с. 13. 2,Прикладна электрохими .Хими , Л,, 1974. 3.Кар кин -Ю. В. и др, Чкстые. химические вещества, М., Хими , 1974, с. 399 (прототип).The aim of the invention is to improve the degree of purification of gin ions, and to increase the yield of the finished product. 3c. The goal is achieved by the fact that, before neutralization, the waste solution B is used to introduce sodium chloride and hp1c1 to the zinc glyoxide sublimation by means of a solution of sodium chloride, and p and m. To the waste solution containing nitric acid with a concentration of 76 g / l and nitric acid zinc 4O g / l (zinc), sodium chloride is added in an amount of 40 g / l. The half solution is treated with a 15% solution of sodium hydroxide to pH-9, 5 and the resulting zinc hydroxide, containing 82 g / l of nitrate ions, is crumbled with a solution of chloroxol (sodium) chlorine with a concentration of 40 g / l. According to a content analysis of citrate ions, it is 0.21 g / l and the yield of roTOF3or-o product (zinc) is 95%. This method provides an increased degree of purification of zinc-containing solutions from nitrate ions and reduces their content from a concentration of 4.4 to 0.21 g / l and also justifies an increase in the yield of the finished product from 68 to 95%. S o rm u l a i p o b r o t o i s Slyusob purification of spent zinc – solor kashche1X) nitric acid solution, which includes neutralization of the canker with 1 gatrom to form a suspension of zinc hydroxide, washing the suspension, preparing an electrolyte from the washed zinc – richhe suspension of electrolyte and isolating zinc electrolysis. Characterized in that, in order to increase the degree of purification from nitrate ions and increase the yield of the finished product, sodium chloride is introduced into the waste solution by neutralization and washing is carried out with a solution of sodium chloride. Sources of information taken into account during examination 1. Devtov N. I. et al. On the issue of cleaning zincographic effluents. Polygraph, 1975, No. 7, p. 13. 2, Applied Electrochemistry. Chemistry, L ,, 1974. 3. Karin Keen -Yu. V. et al., Кksty. Chemicals, M., Himi, 1974, p. 399 (prototype).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU762405854A SU697403A1 (en) | 1976-09-14 | 1976-09-14 | Method of purifying spent zinc-containing nitric acid solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU762405854A SU697403A1 (en) | 1976-09-14 | 1976-09-14 | Method of purifying spent zinc-containing nitric acid solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU697403A1 true SU697403A1 (en) | 1979-11-15 |
Family
ID=20677518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU762405854A SU697403A1 (en) | 1976-09-14 | 1976-09-14 | Method of purifying spent zinc-containing nitric acid solution |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU697403A1 (en) |
-
1976
- 1976-09-14 SU SU762405854A patent/SU697403A1/en active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SU778707A3 (en) | Method of purifying sodium chloride solution | |
| DE69100619T2 (en) | METHOD AND DEVICE FOR THE PROCESSING OF LIQUID WASTE FROM THE PHOTOGRAPHIC DEVELOPMENT. | |
| PL164483B1 (en) | Method of removing nitrogen compounds from liquids and apparatus therefor | |
| CN113582415A (en) | Desalination treatment method of reverse osmosis concentrated water | |
| US4038366A (en) | Method for removing hydrogen sulfide | |
| GB1519571A (en) | Brine purification process | |
| SU697403A1 (en) | Method of purifying spent zinc-containing nitric acid solution | |
| US3788960A (en) | Recycling of ion exchange regenerant chemicals | |
| US4725360A (en) | Working up wastewaters containing hydroxylamine or its salts | |
| SU798050A1 (en) | Method of waste water purification from chlorine | |
| US3639118A (en) | Process for purifying mercury | |
| JPS5581782A (en) | Treatment method for flue gas desulfurization waste water | |
| SU833565A1 (en) | Method of waste water purification from thiosulfate ion | |
| SU633821A1 (en) | Method of purifying solution from mercury | |
| SU893888A1 (en) | Method of treatment of alkaline hypochlorite and acid waste water containing fluorine | |
| SU947072A1 (en) | Process for purifying effluents | |
| SU962213A1 (en) | Method for recovering and regenerating chromium from effluents of leather-making factories | |
| JPS55104632A (en) | Treating method of waste gas containing hydrogen chloride and sulfur oxide | |
| RU2128147C1 (en) | Method of removing hardness ions from water | |
| US4235853A (en) | Method for sulfur dioxide control II | |
| SU827403A1 (en) | Method of regenerating pickling solution containing sulfuric acid and ferric sulfate | |
| RU96112805A (en) | METHOD FOR DISPOSAL OF COPPER-CONTAINING WASTE | |
| SU505610A1 (en) | Method of regenerating activated carbon | |
| KR960013331B1 (en) | Dyeing waste water treatment method | |
| SU1440943A1 (en) | Method of purifying zinc sulfate solutions from copper and cadmium |