SU539093A1 - Method for preparing active chlorine solutions - Google Patents
Method for preparing active chlorine solutionsInfo
- Publication number
- SU539093A1 SU539093A1 SU1863846A SU1863846A SU539093A1 SU 539093 A1 SU539093 A1 SU 539093A1 SU 1863846 A SU1863846 A SU 1863846A SU 1863846 A SU1863846 A SU 1863846A SU 539093 A1 SU539093 A1 SU 539093A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- active chlorine
- preparing active
- chlorine solutions
- electrolysis
- cathode
- Prior art date
Links
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Description
33
нерастворимых продуктов на поверхности катода и скоплени нх в электролизере в количествах , привод щих к нарушению процесса.insoluble products on the cathode surface and accumulations in the electrolyzer in quantities that lead to process disruption.
Предлагаемый способ получени раствора активного хлора электролизом морской воды был проверен в стендовых услови х (на черноморской воде) и в натурных судовых услови х (на океанской воде) на модели иромышленной установки. Длительность стендовых испытаний составила 6000 ч, длительность натурных - свыше 3000 ч.The proposed method of obtaining a solution of active chlorine by seawater electrolysis was tested in bench conditions (on Black Sea water) and in natural conditions of ships (on ocean water) on a model of industrial installation. The duration of the bench tests was 6000 hours, the duration of full-scale tests exceeded 3000 hours.
В результате проведенных испытаний было установлено:As a result of the tests it was found:
вынос частиц нерастворимых продуктов электролиза обеспечиваетс при скорости потока электролита в межэлектродном пространстве не менее 1,5 м/сек;removal of particles of insoluble electrolysis products is provided at an electrolyte flow rate in the interelectrode space of at least 1.5 m / s;
рыхла структура и отсутствие наращивани сло осадка на катоде обеспечиваетс при катодной плотности тока ке менее iOOO loose structure and the lack of build-up of a layer of sediment on the cathode is provided at a cathode current density ke less than iOOO
при указанных параметрах электролиза скоплени осадка в межэлектродном иространстве не происходит, а на поверхности катода наблюдаетс тонкий слой осадка чешуйчатого характера.At the indicated electrolysis parameters, sediment does not accumulate in the interelectrode space, and a thin layer of scaly sediment is observed on the cathode surface.
Ограничени по верхним пределам рассматриваемых параметров обусловлены:The limitations on the upper limits of the parameters considered are due to:
по скорости потока электролита - гидравлическим сопротивлением установки;the flow rate of the electrolyte - hydraulic resistance of the installation;
по плотности тока на катоде - коррозионной стойкостью существуюших электродных гйатериалов ири катодной пол ризации.according to the current density at the cathode - corrosion resistance of existing electrode electrodes and cathodic polarization.
Предлагаемый способ получени раствора активного хлора электролизом морской воды обеспечивает возможность осуществлени длительного стабильного процесса, а следовательно , и надежность защпты от обрастани конструкций, эксплуатирующихс в морской воде.The proposed method for obtaining a solution of active chlorine by the electrolysis of seawater provides the possibility of carrying out a long-term stable process and, consequently, the reliability of the graft from fouling of structures operating in seawater.
Ф о р м у л а и 3 о б р е т е и и Ф орм ул а and 3 о б р е e and u
Способ получени раствора активного хлора электролизом морской воды на твердых электродах ири иепрерывном иотоке электролита между электродами, отличающийс тем, что, с целью обеспечени длительного стабильного процесса, электролиз ведут ири скорости потока морской воды 1,5-10 м/сек и плотности тока ка катоде 1000-5000 А/м.The method of obtaining a solution of active chlorine by electrolysis of sea water on solid electrodes and a continuous flow of electrolyte between electrodes, characterized in that, in order to ensure a long, stable process, electrolysis is carried out and the flow rate of sea water is 1.5-10 m / s and cathode current density 1000-5000 A / m.
Источники информации, прип тые во внимание при экспертизе:Sources of information attributed to the examination:
1. Патеиг США Xs 3536598, кл. 204-128, 1970.1. Pateig USA Xs 3536598, cl. 204-128, 1970.
2. Патент Великобритании № 1104747, кл. С 7В, 1975.2. Patent of Great Britain No. 1104747, cl. From 7B, 1975.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1863846A SU539093A1 (en) | 1972-12-28 | 1972-12-28 | Method for preparing active chlorine solutions |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU1863846A SU539093A1 (en) | 1972-12-28 | 1972-12-28 | Method for preparing active chlorine solutions |
Publications (1)
Publication Number | Publication Date |
---|---|
SU539093A1 true SU539093A1 (en) | 1976-12-15 |
Family
ID=20536994
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU1863846A SU539093A1 (en) | 1972-12-28 | 1972-12-28 | Method for preparing active chlorine solutions |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU539093A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007022572A1 (en) * | 2005-08-22 | 2007-03-01 | Poolrite Equipment Pty Ltd | A pool chlorinator |
-
1972
- 1972-12-28 SU SU1863846A patent/SU539093A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007022572A1 (en) * | 2005-08-22 | 2007-03-01 | Poolrite Equipment Pty Ltd | A pool chlorinator |
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