SU962212A1 - Method for purifying effluents from organic contaminants - Google Patents
Method for purifying effluents from organic contaminants Download PDFInfo
- Publication number
- SU962212A1 SU962212A1 SU792858049A SU2858049A SU962212A1 SU 962212 A1 SU962212 A1 SU 962212A1 SU 792858049 A SU792858049 A SU 792858049A SU 2858049 A SU2858049 A SU 2858049A SU 962212 A1 SU962212 A1 SU 962212A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- conductive material
- silicon carbide
- titanium
- mixture
- organic contaminants
- Prior art date
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/025—Thermal hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F1/46114—Electrodes in particulate form or with conductive and/or non conductive particles between them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Description
(54) СПОСОБ ОЧИСТКИ СТОЧНЫХ ВОД ОТ ОРГАНИЧЕСКИХ ПРИМЕСЕЙ(54) METHOD FOR CLEANING WASTE WATER FROM ORGANIC IMPURITIES
Изобретение относитс к cnoco6ciM очистки сточных вод, содержаи- х органические примеси, и может быть ис-пользовано , например при очистке сточных вод предпр1и тий органического синтеза.The invention relates to sewage treatment cnoco 6ciM containing organic impurities, and can be used, for example, in sewage treatment of organic synthesis preparations.
Известен способ очистки сточных вод от органических примесей путем обработки их в слое зернистого токопровод щего материала, помещенного в межэлектролизное пространство пол электрического тока, причем в качестве электропроводного материала могут быть использованы.гранулы алюмини , карбида кремни , наход щегос в псевдоожиженном состо нии при подаче в межэлектродное пространство кислородсодержащего гаэа 1.A known method of purifying wastewater from organic impurities by treating them in a layer of granular conductive material placed in the interelectrolytic space of an electric current field, and granules of aluminum, silicon carbide, which is in a fluidized state when fed into, can be used as an electrically conductive material. interelectrode space of oxygen-containing gaea 1.
Недостатком известного способа вл етс значительный расход электроэнергии на (5-10 кВт.ч/м, а кроме того, невысока степень очистки.The disadvantage of this method is a significant energy consumption of (5-10 kWh / m, and in addition, the low degree of purification.
Цель изобретени - повышение степени очистки сточных вод, содержащих органические примеси и снижение энергозатрат на проведение процесса.The purpose of the invention is to increase the degree of purification of wastewater containing organic impurities and reduce energy consumption for the process.
Поставленна цель достигаетс тем, что при обработке сточных вод в слое зернистого токопровод щегоThe goal is achieved by the fact that during the treatment of wastewater in the layer of granular conductive
материала, помещенного в межэлектродное пространство пол электрического тока с подачей кислородсодержащего газа, в качестве зернистого токопровод щего материала используют смесь частиц титана и карбида кремни при следующем соотношении компонентов , вес.%;a material placed in the interelectrode space of an electric current field with an oxygen-containing gas supply, a mixture of titanium and silicon carbide particles is used as a granular conductive material in the following ratio of components, wt.%;
Титан12-15Titan12-15
10ten
Карбид кремни 85-88 Используют токопрговод щий материал с размером частиц 4-5 мм.Silicon carbide 85-88 A current-carrying material with a particle size of 4-5 mm is used.
Применение гранул алюмини или гранул сшюмини в смеси с карбидом The use of aluminum granules or granules with shyumini mixed with carbide
15 кремни не обеспечивает продолжительности работы установки в св зи с тем, что гранулы алюмини в процессе работы окисл ютс и на их поверхности образуетс нетокопровод сда 15, the silicon does not ensure the duration of the plant operation due to the fact that aluminum granules in the process of operation are oxidized and a non-conductor is formed on their surface.
20 прочна окисна пленка, преп тствующа образованию электроразр дов. . Дл удалени последней требуетс дополнительна периодическа химическа обработка (через каждые 1025 12 ч). Алюминий относитс к амфотерным метгшлам и в агрессивных (кислых и щелочных водах) подвержен разрушению. В св зи с этим в предлагаемом способе рекомендуетс ис- 20 strong oxide film that prevents the formation of electric discharges. . Additional periodic chemical treatment is required to remove the latter (every 1025–12 hours). Aluminum refers to amphoteric trash and in aggressive (acidic and alkaline waters) is susceptible to destruction. In this regard, in the proposed method, it is recommended to use
30 J oльзoвaть гранулы титана, который не подвергаетс окислению и коррозионно стоек к агрессивным средам. Титан рекомендуетс использовать в смеси с карбидом кремни . Соотношение смеси, состо щей из 12-15% титана и 88-85% карбида крем ни , найдено экспериментально. Такое соотношение позвол ет снизить в цепом электросопротивление всей загрузки в 1,5-2 раза. Произвольной варьирование соотношени металла в загрузке не дает желаемого эффекта очистки. При увеличении содержани металла от 15 и более процентов воз можно образование короткого замыкани , во избежание которого требуетс включение в электрическую цепь дoпoлi итeльнoгo сопротивлени , что приводит к большому расходу электро энергии. Увеличение размера зерен свыше 5 мм не. позвол ет создать кип щее состо ние (псевдоожиженное) токопровод щей загрузки. Следовател но, искрообразование отсутствует, загрузка работает как токопроводник30 J Titanium granules, which are not subject to oxidation and corrosion-resistant to aggressive media. Titanium is recommended to be used in a mixture with silicon carbide. The ratio of the mixture consisting of 12-15% titanium and 88-85% silicon carbide was found experimentally. This ratio reduces the electrical resistance of the entire load in the circuit by 1.5-2 times. Arbitrary variation of the metal ratio in the load does not give the desired cleaning effect. With an increase in the metal content of 15 percent or more, a short circuit can be formed, to avoid which it is necessary to add a full resistance to the electrical circuit, which leads to a large consumption of electrical energy. An increase in grain size above 5 mm is not. allows you to create a boiling state (fluidized) conductive load. Consequently, sparking is absent, loading works as a conductor
Смесь fкарбид кремни + титан) 15% Ti размер гранул 4-5 ммA mixture of silicon carbide (titanium + titanium) 15% Ti granule size 4-5 mm
Смесь (SiC+Ti)Mixture (SiC + Ti)
15 6-f15 6-f
Смесь (SiC+Ti) 15% Ti 1-3 ммA mixture of (SiC + Ti) 15% Ti 1-3 mm
Таблица 1Table 1
1024 92,41024 92.4
3-53-5
2020
3-53-5
10241024
1.0241.024
2020
3-53-5
876876
10241024
20 окисление загр знений не происходит, Эффект очистки равен нулю. Уменьшение размера зерен менее 4 мм приводит к выносу загрузки из реакционной зоны очистительного аппарата. В св зи с этим происходит уменьшение количества токопровод щей загрузки , а следовательно, уменьшение общего количества искрообразований в реакционной зоне, что отрицательно вли ет на эффект очистки. Сравнительные данные приведены в табл. 1. Результаты опытов представлены в табл. 2. Как следует из представленных данных, применение предлагаемого способа позвол ет снизить расход энергии в 1,5-2 раза и повысить степень очистки сточных вод от растворенных органических примесей, что дозвол ет использовать их в оборотном водоснабжении и предотвратить загр знение окружающей среды.20 no oxidation of contamination occurs, the cleaning effect is zero. A decrease in the grain size of less than 4 mm leads to the removal of the load from the reaction zone of the cleaning apparatus. In this connection, there is a decrease in the amount of conductive load and, consequently, a decrease in the total number of sparks in the reaction zone, which negatively affects the cleaning effect. Comparative data are given in Table. 1. The results of the experiments are presented in table. 2. As follows from the presented data, the application of the proposed method makes it possible to reduce energy consumption by 1.5–2 times and to increase the degree of purification of wastewater from dissolved organic impurities, which makes it possible to use them in circulating water supply and to prevent pollution of the environment.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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SU792858049A SU962212A1 (en) | 1979-12-25 | 1979-12-25 | Method for purifying effluents from organic contaminants |
Applications Claiming Priority (1)
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---|---|---|---|
SU792858049A SU962212A1 (en) | 1979-12-25 | 1979-12-25 | Method for purifying effluents from organic contaminants |
Publications (1)
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SU962212A1 true SU962212A1 (en) | 1982-09-30 |
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SU792858049A SU962212A1 (en) | 1979-12-25 | 1979-12-25 | Method for purifying effluents from organic contaminants |
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SU (1) | SU962212A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1167299A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Apparatus and method for hydrothermal electrolysis |
EP1166852A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Method and apparatus for treatment of gas by hydrothermal electrolysis |
EP1167298A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Method and apparatus for treating aqueous medium |
-
1979
- 1979-12-25 SU SU792858049A patent/SU962212A1/en active
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1167299A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Apparatus and method for hydrothermal electrolysis |
EP1166852A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Method and apparatus for treatment of gas by hydrothermal electrolysis |
EP1167298A4 (en) * | 1999-02-10 | 2002-08-21 | Ebara Corp | Method and apparatus for treating aqueous medium |
US6572759B1 (en) | 1999-02-10 | 2003-06-03 | Ebara Corporation | Method and apparatus for treating aqueous medium |
US6585882B1 (en) | 1999-02-10 | 2003-07-01 | Ebara Corporation | Method and apparatus for treatment of gas by hydrothermal electrolysis |
US6939458B1 (en) | 1999-02-10 | 2005-09-06 | Ebara Corporation | Apparatus and method for hydrothermal electrolysis |
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