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1. The procurement cost can be reduced by 3%.
2. The electric current efficiency can be increased by 3% or above.
3. Cell voltage can be reduced by 0.05 ~ 0.10V.
4. The current density can be increased to 350-400A/m2 during the copper electrowinning process.
1. The plate surface is flat, and the alloy composition is evenly distributed.
2. Embossing was added as a surface treatment process, which enhances the corrosion resistance of the anode plates while reducing the lead content in the cathode copper.
3. Holes are on the plate which makes that the electrolyte has good fluidity.
1. The procurement cost can be reduced by 5%.
2. The electric current efficiency can be increased by 2-5%.
3. The maximum current density can exceed 800A/m2.
4. The DC current cost is reduced by 110 ~ 250KWh/ton of zinc production.
1. It is made of multi-element lead alloy (containing rare earth elements).
2. The plate surface is flat, and the alloy composition is evenly distributed.
3. Hot rolling first, and then cold rolling.
4. The surface is covered by a layer of ceramic material, which enhances the corrosion resistance.
1. The hanger bar of the cathode plate is made of T2 copper, and the purity of copper is 99.90%.
2. The copper bar is tightly surrounded by the stainless-steel tube. The plate surface finish level is 2B.
3. The electric resistance between the copper conductive end and a point on the center line of bottom of the plate is less than or equal to 0.5 mΩ
1. The hanger bar is made from a whole-body aluminum block.
2. The cathode plate is made from aluminum alloy 1070, Al ≥ 99.7%, HBS: 32-35.
3. The copper conductive end is friction welded to hanger bar.
4. The liquid level part of the plate is coated with anti-corrosion material. The plate surface finish level is 2B.
Discussion for Upper Drawing:
1. Anode weight is 152kg based on the drawing. Section area 25*25(mm) cannot bear the weight.
2. If you prefer to 12mm thick, we suggest to use section area in 25*50(mm).
3. Also we recommend 5 mm thickness for lead sheating.
Discussion for Lower Drawing:
1. There is no holes on your anode plate drawing.
2. We recommend with 12 holes. Thus, the electrolyte has good fluidity and avoids the risk of short circuit.
3. Moreover, the 8 holes marked in red are fitted with insulators.
ANSWER: We, PRS, have 20 years of rich experience in the production of copper and zinc electrowinning (EW) equipment.
The excellent quality of our products comes from the following points:
1. Senior engineers make perfect design.
2. Unique high-tech patents are applied in anode plate and cathode plate to increase current efficiency.
3. Experienced workers for production.
4. Using high-quality raw material: the stainless steel materials of plates for cathode are made by TISCO or POSCO; the materials of plates for anode are made of high purity of lead (99.99%) and tin (99.96%).
ANSWER: Whether your mines or plant is big or small, we will support you in all aspects.
For increasing your profits and reducing your costs, we can support you in the following points:
1. Our annual output of 600,000 pieces is very large, so we can well control the cost of raw materials and production, which can help you reduce your procurement costs.
2. The new fence-type anode plate supported by our high-tech patent can help you reduce the procurement cost by 3% and increase production capacity by 3%~5%.
3. Our reasonable customized design of anode plate can increase electrolyte fluidity and improve current efficiency by 3%.
4. Cathodic plates can reduce losses with surface finish of level 2B when stripping cathode copper and zinc.
ANSWER: MOQ in 100 pieces of anode or cathode plate. It's easier to kickstart your business.
ANSWER:
1. Put the anode plates and cathode plates into a stainless steel square frame, and then cover the frame with a thin steel plate to ensure moisture-proof, rust-proof, acid-proof, salt-alkali-proof, and collision-proof, suitable for international shipping and rough loading and unloading.
2. If you purchase the electrolytic cells at the same time as the anode and cathode plates, we will put the anode and cathode plates into the cells and then pack them for delivery in order to save the transportation cost, so as to reduce the use of containers.
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