chlor alkali plant titanium anode box RuO2 IrO2 coating titanium anode box titanium anode box

Product Overview

Description

Item Name	Titanium anode tray for chlor-alkali industry
Size (MM)	Tray Size: 20*960*960MM  40*480*1040MM or as per  Titanium Mesh Size: 1.5*887*887 Baffles: Gr2 Ti Plate: Thk 2.0MM
Material	Gr2 Pure Titanium ASTM Standards
Coating	TiO2/RuO2 / RuO2-IrO2 Coating Thk: 20-25 um 12g/M2
Operation Current	3500A/M2
Fluids	1. Saturated NaCl brine at PH 2 to 4 2. Wet Chlorine gas 3. Depleted NaCl brine 4. Minor concentrations of NaClO3 and NaClO
Working Temperature	80-85 C
Membranes	920MM*920MM*250um

 

Titanium anode for chlor alkali industry            
1. Working conditions: Saturated NaCl (35%) solution
2. Current density: 1000A/m2
3. Electrolysis method: ion-exchange membrane electrolysis (anode chamber and cathode chamber)
4. Coating type: RuO2-IrO2 or RuO2-TiO2 +titanium base
5. Service life: more than 5 years
6. Electrochemical performance and life test (20000A/m2)
7. Reference standard : HG/T2471-2007 Q/CLTN-2012
Product Name Strengthen weightlessness mg Polarizabilitymv Chlorine evolution potential V Test Conditions
RuO2-IrO2 titanium anode ≤10 40

Product use background and introduction           
       Caustic soda is produced by electrolysis of salt water solution, chlorine is produced at the anode, and hydrogen and caustic soda are produced by reaction at the cathode. The use of our company's coated electrodes in the production of chlor-alkali has the advantages of low loss, greatly reduced chlorine evolution potential compared with graphite electrodes, and stable size and shape. Compared with graphite electrodes, the product quality is higher, lower energy consumption and higher chlorine purity in the same electrolysis environment.

Product Name Strengthen weightlessness mg Polarizabilitymv Chlorine evolution potential V Test Conditions
RuO2-IrO2 titanium anode ≤10 40

 

 

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