OXITRON – is a family of devices for precision electrochemical oxidation and reduction of organic and inorganic substances in various technological processes. Pre-production models or devices lot can be produced. Orders are taken for OXITRON devices production as applied to the concrete technological process.
OXITRON-C-07-01 is a device for electrochemical oxidation of organic pharmaceutical medications and chemicals.
Technical characteristics
| Productivity , l / h |
10-45 |
| Effective current in reactor, A |
up to 500 |
| Concentration of oxidizable organic substances in the solution, %, no less than |
1 |
| Power consumption at typical operation, Wt, no more than |
2200 |
Rating values of electrical parameters of reactor of electrochemical unit
- - current strength , A
- - voltage , V
|
60 - 110
16 - 20 |
| Nominal gas pressure in anode chamber of reactor of electrochemical unit, atm. |
0,01 – 0,50 |
| Mass of the device in complete set, kg, no more than |
400 |
| Overall dimensions , mm |
1500x600x2000 |
The complete set of the device includes electrochemical unit, power supply unit and control unit placed together on the same frame, dosing pump for organic substances solution supply placed at the front panel of electrochemical unit, pump for solution supply into foam suppressor, tanks (50 l) for initial solution preparing and for collecting of oxidation products. The main part of the device is electrochemical reactor composed 16 flow-through diaphragm electrochemical module elements MB-26 connected hydraulically parallel by upper and lower cathode and anode collectors. Upper and lower collectors of cathode chamber connect hydraulically parallel with heat exchanger and make cathode flow circuit, which outlet is in upper cathode collector and connected with separator Е3 for gas (hydrogen) separation off liquid (catholyte). Peltie cooler is for cooling catholyte circulated through it.
Principal hydraulic scheme of OXITRON-C-07-01 device
ПГ- form breaker;
Е2- tank for oxidation products;
РПЭ- flow-through electrochemical reactor;
Е3- tank for catholyte of cathode flow circuit;
В5- anolyte valve;
В6- catholyte valve;
Н1- dosing pump;
В3- oxidation products valve;
В2- valve of solution supply to anode chamber;
В4- valve of catholyte by-way;
Е1- tank for initial solution;
В1- valve of anolyte circulation;
В7- valve of solution supply to foam breaker;
Н2- pump of foam breaker.
OXITRON–R-07-01 is a device for electrochemical treatment of electrolyte water solutions for regulation of its chemistry and reactivity. In particular, the device is developed for technology of ammonia removing from manufacturing water of nuclear power plants. Performance test was successfully carried out. Проведены успешные промышленные испытания. Serial production is prepared.
Appearance of OXITRON-R-07-01 device
1 – control unit;
2 – power supply unit;
3 – power cord (attached to control unit);
4 – аamperemeter;
5 – voltmeter;
6 – line of anolyte outlet;
7 – line of catholyte outlet;
8, 9 - manometer;
10 – power cord from control unit to network system 220 V;
11 – frame;
12 – unit of electrochemical reactors;
13 – connecting pipe of inlet of manufacturing treated water into anode chamber;
14 - connecting pipe of inlet of manufacturing treated water into cathode chamber;
15 – connecting pipe of anolyte and catholyte discharge;
16 – valve "Catholyte discharge";
17 – valve "Anolyte discharge".
Technical characteristics
| Productivity of anode treated solution (anolyte), l/h |
1500 |
| Productivity of cathode treated solution (catholyte), l/h |
1500 |
| Concentration of electrolytes in initial solutions, g/l |
10 – 100 |
| Power consumption at typical operation, Wt, no more than |
2000 |
Rating values of electrical parameters of reactor of electrochemical unit
- - current strength , A
- - voltage , V
|
|
| Effective value of current, A |
240 – 480 |
| Mass of the device in complete set, kg, no more than |
70 |
The main part of the device is electrochemical reactor composed 16 flow-through diaphragm electrochemical module elements MB-26 connected hydraulically parallel by upper and lower cathode and anode collectors.
Principal hydraulic scheme. Device use in system of ammonia removing from manufacturing water
Е1 – tank for water disinfection;
Е2 – tank of idler circuit;
У1, У2 – cross-flow sensors;
Ф1,Ф2 – filter;
МН1 – manometer of pressure control in anode chamber of reactor;
МН2 – manometer of pressure control in cathode chamber of reactor;
РПЭ1-РПЭ16 – flow-through electrochemical module reactor of 16 elements MB-26 connected together;
Н1 – pump of anode flow circuit;
Н2 – pump of cathode flow circuit;
ВН1 – valve for anolyte discharge;
ВН2 – valve for catholyte discharge.
OXITRON–M-07-01 is a device for anode electrochemical treatment of water solutions of hydrochloric acid for regulation of its chemistry and reactivity.
Technical characteristics
| Productivity of anolyte, l/h |
20 - 140 |
| Productivity of catholyte, l/h |
4,0-10,0 |
| Concentration of initial solution of hydrochloric acid, % |
1 – 5 |
| Power consumption at typical operation, Wt, no more than |
1500 |
Rating values of electrical parameters of reactor of electrochemical unit
- - current strength , A
- - voltage , V
|
|
| Working pressure in anode chamber, atm. |
0,2-0,5 |
| Mass of the device in complete set, kg, no more than |
70 |
| Overall dimensions , mm |
350x640x1860 |
The complete set of the device includes electrochemical unit, power supply unit and control unit placed together on the same frame. The main part of the device is electrochemical reactor composed 16 flow-through diaphragm electrochemical module elements MB-26 connected hydraulically parallel by upper and lower cathode and anode collectors.
Principal hydraulic scheme of device
М1- manometer of pressure control in anode chamber of reactor;
РД2 – pressure regulator on anode circuit;
КАВ – upper anode collector;
ВН7 – valve "Atmosphere/rinse";
БС – quick disconnect;
Д – drainage;
ККВ – upper cathode collector;
СПК- catholyte separator;
ВН1 – valve of cooling water supply to device (is not in complete set);
ККН – lower cathode collector;
ВН2 – valve "cathode chamber filling";
ВН3 – valve of rapid supply of acid solution into anode chamber;
ВН4 – valve of acid solution supply from tank (is not in complete set);
Н2 – pump of electrolyte solution supply for rapid filling of anode chamber (is not in complete set);
Н1 – membrane pump of electrolyte solution supply to reactor;
ВН5 – valve of anolyte discharge;
ВН6 – valve of catholyte discharge;
КАН – lower anode collector.
Acid solution is supplied at operating mode into anode chamber of reactor by membrane pump Н1. Additional pump Н2 provides with rapid supply of acid solution into anode chamber during period of reactor filling. Outlet of upper anode collector is connected with pressure regulator of anode chamber of reactor, through which all the treated hydrochloric acid solution goes.
