This page explains how Anodizing Tank Module is classified within Fabricated Metal Product Manufacturing. Technical values and manufacturer relationships are research references; confirm the current specification and supplier evidence for each order.
A modular tank unit for the electrochemical anodizing of aluminum profiles, containing electrolyte and electrodes.
Technical details and manufacturing context for Anodizing Tank Module
| Parameter | Typical range | Notes & selection driver |
|---|---|---|
| Tank Material | Polypropylene (PP) or Fiberglass Reinforced Plastic (FRP) | Polypropylene (PP) or Fiberglass Reinforced Plastic (FRP) — PP for chemical resistance and cost; FRP for higher structural strength. PP for chemical resistance and cost; FRP for higher structural strength.ASTM D4101 for PP, ASTM D3917 for FRP |
| Tank Wall Thickness | 10–20 mm | 10–20 — Thicker walls for larger tanks or higher temperatures. Thicker walls for larger tanks or higher temperatures. |
| Working Volume | 500–5000 L | 500–5000 — Depends on production capacity; larger volumes for higher throughput. Depends on production capacity; larger volumes for higher throughput. |
| Temperature Range | 15–25 °C | 15–25 — Optimal for sulfuric acid anodizing; outside range affects coating quality. Optimal for sulfuric acid anodizing; outside range affects coating quality. |
| Temperature Control Accuracy | ±1 °C | ±1 — Required for consistent oxide layer thickness. Required for consistent oxide layer thickness. |
| Electrolyte Concentration (Sulfuric Acid) | 150–200 g/L | 150–200 — Typical for Type II anodizing. Typical for Type II anodizing.ASTM B580 |
| Electrode Material | Lead or Titanium coated with mixed metal oxide (MMO) | Lead or Titanium coated with mixed metal oxide (MMO) — Lead for cost; MMO for longer life and lower maintenance. Lead for cost; MMO for longer life and lower maintenance. |
| Electrode Spacing | 100–300 mm | 100–300 — Affects current distribution and coating uniformity. Affects current distribution and coating uniformity. |
| Heating/Cooling Capacity | 5–20 kW | 5–20 — To maintain temperature within range; depends on ambient and heat generation. To maintain temperature within range; depends on ambient and heat generation. |
| Agitation System | Air agitation or pump circulation | Air agitation or pump circulation — Ensures uniform temperature and concentration. Ensures uniform temperature and concentration. |
| Exhaust System Connection | DN100–DN200 mm | DN100–DN200 — For fume extraction; size depends on tank width. For fume extraction; size depends on tank width. |
| Drain Valve Size | DN50–DN80 mm | DN50–DN80 — For quick draining and maintenance. For quick draining and maintenance. |
| Lining Material | PVC or PP lining for steel tanks | PVC or PP lining for steel tanks — If tank is steel, lining protects against corrosion. If tank is steel, lining protects against corrosion. |
| Service Life | 10–15 years | 10–15 — With proper maintenance and within operating conditions. With proper maintenance and within operating conditions. |
| Duty Cycle | Continuous | Continuous — Designed for 24/7 operation. Designed for 24/7 operation. |
| Electrolyte Temperature | 15–25 °C | 15–25 °C — Outside this window: Below 15°C: reduced coating thickness and hardness; above 25°C: porous coating, reduced corrosion resistance. Outside this window: Below 15°C: reduced coating thickness and hardness; above 25°C: porous coating, reduced corrosion resistance. |
| Sulfuric Acid Concentration | 150–200 g/L | 150–200 g/L — Outside this window: Below 150 g/L: low conductivity, uneven coating; above 200 g/L: excessive etching, rough surface. Outside this window: Below 150 g/L: low conductivity, uneven coating; above 200 g/L: excessive etching, rough surface. |
| Current Density | 1.5–3.0 A/dm² | 1.5–3.0 A/dm² — Outside this window: Below 1.5: thin coating; above 3.0: burning, powdery coating. Affects coating thickness and hardness.ASTM B580 |
| Voltage | 12–24 V DC | 12–24 V DC — Outside this window: Below 12V: insufficient current; above 24V: risk of arcing and damage to coating. Depends on tank size and electrode spacing. |
| Electrolyte Level | 80–90% of tank height | 80–90% of tank height — Outside this window: Low level: exposes electrodes, uneven current; high level: overflow, dilution. Outside this window: Low level: exposes electrodes, uneven current; high level: overflow, dilution. |
Ranges are indicative industry figures for RFQ preparation, not a supplier commitment. Confirm every value and standard with the legal manufacturer before ordering.
Indicative industry ranges for design and RFQ preparation. Confirm the exact figures and applicable standard with the manufacturer before specifying.
Quoted from the published standard.
Manufacturer profiles associated with Anodizing Tank Module.
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A practical evidence checklist for RFQ preparation and supplier evaluation.
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The tank can be made of polypropylene (PP) or fiberglass reinforced plastic (FRP), with stainless steel 316L and PVC also listed as materials on file. The choice depends on chemical resistance and structural strength requirements. For steel tanks, a PVC or PP lining is used for corrosion protection.
The working volume ranges from 500 to 5000 liters, depending on production capacity. Larger volumes are used for higher throughput. The exact volume should be confirmed based on the specific production line requirements.
Standards referenced include ASTM B580 for anodizing, ASTM D4101 for polypropylene, and ASTM D3917 for fiberglass reinforced plastic. These are procurement references and do not guarantee compliance; verify with the manufacturer.
The recommended electrolyte temperature range is 15–25 °C. Outside this range, coating quality may be affected: below 15 °C reduces coating thickness and hardness, while above 25 °C leads to porous coating and reduced corrosion resistance.
Editorial classification, named public sources where available, and source-reviewed manufacturer records.
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