SU833566A1 - Method of purifying return waste water - Google Patents
Method of purifying return waste water Download PDFInfo
- Publication number
- SU833566A1 SU833566A1 SU792815058A SU2815058A SU833566A1 SU 833566 A1 SU833566 A1 SU 833566A1 SU 792815058 A SU792815058 A SU 792815058A SU 2815058 A SU2815058 A SU 2815058A SU 833566 A1 SU833566 A1 SU 833566A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- mixture
- siderite
- purification
- suspended substances
- coagulants
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 11
- 239000002351 wastewater Substances 0.000 title claims description 6
- 239000000203 mixture Substances 0.000 claims description 12
- 239000000126 substance Substances 0.000 claims description 10
- 229910021646 siderite Inorganic materials 0.000 claims description 8
- 239000000701 coagulant Substances 0.000 claims description 7
- 238000000746 purification Methods 0.000 claims description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 235000019353 potassium silicate Nutrition 0.000 claims description 4
- 159000000014 iron salts Chemical class 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 238000004065 wastewater treatment Methods 0.000 claims description 2
- 230000001112 coagulating effect Effects 0.000 claims 1
- 239000007787 solid Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical class [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 3
- 238000005352 clarification Methods 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 229910052742 iron Chemical class 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000010414 supernatant solution Substances 0.000 description 1
Landscapes
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Description
(54) СПОСОБ ОЧИСТКИ ОБОРОТНЫХ СТОЧНЫХ ВОД(54) METHOD FOR CLEANING REVERSE SEWAGE WATER
1one
Изобретение относитс к способам очистки сточных вод от взвешенных веществ и может быть использовано дл осветлени оборотных стоков обогатительных и металлургических производсThe invention relates to methods for the treatment of wastewater from suspended substances and can be used to lighten the circulating effluents of enrichment and metallurgical production.
Известен способ очистки сточных вод, содержащих взвешенные вещества с помощью смеси солей алюмини и железа i.A known method of purification of wastewater containing suspended solids using a mixture of salts of aluminum and iron i.
Недостатком способа вл етс неудовлетворительна , степень очистки растворов, содержащих взвешенные частицы, пептизированные жидким стеклом . .The disadvantage of the method is unsatisfactory, the degree of purification of solutions containing suspended particles, peptized with liquid glass. .
аbut
Цель изобретени - повУшёние степени очистки от взвешенных веществ, пептизированных жидким стеклом.The purpose of the invention is to improve the degree of purification from suspended substances, peptized with liquid glass.
Поставленна цель достигаетс с помощью коагул нтов смеси солей алюмини и железа, а в качестве коагул нтов используют смесь, содержащую двойную соль алюмини AlClg- HSQj и природный сидерит.This goal is achieved using coagulants of a mixture of aluminum and iron salts, while coagulants use a mixture containing the double aluminum salt AlClg-HSQj and natural siderite.
Сидерит перед использованием подвергают обжигу с поваренной солью при 400-500°С.Siderite before use is subjected to roasting with sodium chloride at 400-500 ° C.
Кроме того, коагулирукийую смесь ввод т из расчета 6-20% от веса взвеlUGHHHX веществ при соотношении компонентов Altl2.-HS04 и природного сидерита , равном 1-2:1.In addition, the coagulated mixture is introduced at the rate of 6–20% of the weight of the LUGHHHX substances with a ratio of Altl2 to HS04 and natural siderite equal to 1-2: 1.
Способ иллюстрируетс следующими примерами..The method is illustrated by the following examples.
Пример 1. Оборотные сточные воды обогатительного передела, содержащие до 600 г/м взвешенных веществ , пептизированн{з1Х жидким стеклом , обрабатывают смесью, содержащей A1C12-HS04 и природный сидерит в весовом соотношении 1:1 из расчета 80 г/м Л Пульпу отстаивают в течение 1 ч. При этом осветленна часть стоков в количестве 78,2% содержит в среднем 30,4 г/м взвешеннЫх веществ. В отсто вшемс растворе содержание твердой части составл ет 3%, воды 97,0%. Обща степень очистки стоков от взвешенных частиц 95%, степень очистки по известному способу до 70-80%.Example 1. Circulating wastewater from the processing plant, containing up to 600 g / m of suspended solids, peptized (liquid glass), is treated with a mixture containing A1C12-HS04 and natural siderite in a 1: 1 weight ratio at a rate of 80 g / m L Pulp is settled into for 1 hour. At the same time, the clarified part of the effluent in the amount of 78.2% contains on average 30.4 g / m suspended substances. In the supernatant solution, the solids content is 3%, water 97.0%. The overall degree of wastewater treatment from suspended particles is 95%, the degree of purification by a known method is up to 70-80%.
Пример 2. Оборотные сточные воды с.содержанием взвешенных вещест аналогично примеру 1 обрабатывают смесью минеральных коагул нтов, содержащей сидерит, подвергнутый в течение 40 мин сегрегирующему обжигу с NaCI при 400-500°С. Смесь, содержащую компоненты при соотношении 1:1, ввод т из расчета 80 г/мЛ После часExample 2. Circulating wastewater with the content of suspended substances analogously to example 1 is treated with a mixture of mineral coagulants containing siderite, subjected to segregating roasting for 40 min with NaCI at 400-500 ° С. A mixture containing components at a 1: 1 ratio is introduced at the rate of 80 g / ml. After an hour
отсто осветленна часть стоков составл ет 82%, в ней содержитс в среднем 18,6 г/мвзвешенных веществ. В отсто вшемс растворе содержание твердой части составл ет 3,8%, воды 96,2%, обща степень очистки составл ет 97,0%.Of these, the clarified part of the effluent is 82%, it contains on average 18.6 g / m-weighed substances. In the sludge solution, the solids content is 3.8%, water is 96.2%, the total degree of purification is 97.0%.
В табл.1 показано вли ние расхода смеси коагул нтов и соотношени компонентов в нем на показатели осветлени при соотношении солей и железа ;, врем отстаивани 4 г, сидерит обожженный.Table 1 shows the effect of the consumption of a mixture of coagulants and the ratio of components in it on the indicators of clarification at a ratio of salts and iron; the settling time is 4 g, it is burned.
Таблица 1Table 1
В табл.2 представлены результаты опытов по вли нию соотношени солей алюмини и железа на осветление воды при расходе смеси коагул нтов 20% от веса взвешенных веществ, времени отстаивани 4 ч, сидерит обожженный.Table 2 presents the results of experiments on the effect of the ratio of aluminum and iron salts on water clarification at a flow rate of a coagulant mixture of 20% by weight of suspended solids, settling time 4 h, burned siderill.
Таблица 2table 2
200200
6868
0,5:10.5: 1
Применение предлагаемого способа обеспечивает высокую степень рчистки растворов, пептизированных жидким с теклом.The application of the proposed method provides a high degree of cleaning solutions, peptized liquid with Tekla.
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU792815058A SU833566A1 (en) | 1979-09-11 | 1979-09-11 | Method of purifying return waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU792815058A SU833566A1 (en) | 1979-09-11 | 1979-09-11 | Method of purifying return waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU833566A1 true SU833566A1 (en) | 1981-05-30 |
Family
ID=20848618
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU792815058A SU833566A1 (en) | 1979-09-11 | 1979-09-11 | Method of purifying return waste water |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU833566A1 (en) |
-
1979
- 1979-09-11 SU SU792815058A patent/SU833566A1/en active
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