Engineered for safe, reliable transfer of aggressive acids and alkalis. Fluoropolymer-lined construction or high-performance alloys provide exceptional resistance to sulfuric acid, hydrochloric acid, nitric acid, caustic soda, and other corrosive chemicals.
A comprehensive examination of the engineering, material science, and design features of our acid and alkali resistant pump range.
The Acid and Alkali Resistant Pump is purpose-engineered for the safe transfer of highly corrosive chemicals in industrial processes. Pumping aggressive acids such as sulfuric acid (H2SO4), hydrochloric acid (HCl), nitric acid (HNO3), and hydrofluoric acid (HF) requires specialized materials that resist chemical attack. Similarly, strong alkalis such as sodium hydroxide (NaOH) and potassium hydroxide (KOH) demand corrosion-resistant construction. Our pumps employ two primary technologies for corrosion resistance: fluoropolymer-lined construction and high-performance alloys. Each approach has advantages depending on the chemical concentration, temperature, and pressure requirements of the application.
Fluoropolymer-lined pumps provide exceptional chemical resistance at a lower cost than high-performance alloys for many applications. The pump casing is constructed from carbon steel or ductile iron for structural strength. A liner of PTFE (polytetrafluoroethylene), PFA (perfluoroalkoxy), or PVDF (polyvinylidene fluoride) is molded inside the casing, creating a barrier between the metal structure and the corrosive fluid. PTFE is chemically inert to virtually all chemicals except molten alkali metals and fluorine gas. PFA offers similar chemical resistance with better high temperature performance (up to 180°C). PVDF provides excellent resistance to acids, alkalis, and solvents at a lower cost but with a lower temperature limit (120°C). The liner thickness is typically 3 to 5mm, providing a long service life even in aggressive service.
High-performance alloy pumps are specified when temperatures exceed the limits of fluoropolymer linings or when the fluid is not compatible with fluoropolymers. Alloy options include stainless steel (SS304, SS316, SS316L), duplex stainless steel (2205, 2507), Hastelloy (C276, B2, C22), titanium (Grade 2, Grade 7, Grade 12), and zirconium. Each alloy has specific corrosion resistance characteristics. SS316 provides good resistance to many acids and alkalis but is attacked by chlorides and reducing acids. Hastelloy C276 provides excellent resistance to wet chlorine, hypochlorite, and mixed acids. Titanium is outstanding for seawater and oxidizing acids. Our metallurgists assist in selecting the optimal alloy for your specific chemical concentration and temperature.
The pump hydraulic design is optimized for chemical service. For lined pumps, the impeller is of the semi-open or open type, as the thickness of the lining affects internal clearances. The impeller is manufactured from the same fluoropolymer material or from high-performance alloy. For alloy pumps, enclosed impellers with close-clearance wear rings provide maximum efficiency. The volute casing is designed with smooth transitions to minimize turbulence and erosion of the corrosion-resistant layer. For lined pumps, the casing includes a conductive carbon-filled PTFE layer to dissipate static electricity when pumping flammable solvents.
Material traceability is critical for chemical pumps. Every casting is accompanied by a material test certificate (EN 10204 3.1 or 3.2) documenting chemical composition and mechanical properties. Positive Material Identification (PMI) is performed on all alloy components to verify alloy grade. This is especially important when multiple alloys are used in the same facility, as visual inspection cannot distinguish between SS304 and SS316 or between SS316 and Hastelloy.
The shaft sealing system must prevent leakage of hazardous chemicals to the atmosphere. For most chemical applications, we offer double mechanical seals (API 682 Arrangement 2 or 3) with a pressurized barrier fluid. The barrier fluid is contained in a sealed reservoir, and any leakage is contained rather than released. For applications where absolutely zero leakage is mandatory, we offer magnetic drive (sealless) pumps. The magnetic drive eliminates the dynamic shaft seal entirely, with the impeller driven through a containment shell. This provides the highest level of containment for toxic, carcinogenic, or valuable chemicals.
The pump is available in end-suction, horizontal, or vertical configurations. End-suction pumps are the most common for chemical transfer applications. Horizontal split-case pumps are used for higher flow rates. Vertical in-line and vertical sump pumps are available for tank and sump applications. The configuration is selected based on the installation requirements and available NPSH.
In summary, the Acid and Alkali Resistant Pump delivers safe, reliable, long-lasting service in the most aggressive chemical environments.
Complete performance and material parameters for the acid and alkali resistant pump range.
| Parameter | Specification |
|---|---|
|
Pump Configuration
|
End-suction horizontal / Split-case / Vertical in-line / Vertical sump |
|
Flow Rate Range
|
2 to 800 m³/h (9 to 3,500 US gpm) |
|
Total Head Range
|
10 to 100 meters (33 to 328 feet) |
|
Fluid Temperature (Lined)
|
PTFE: -20°C to +120°C / PFA: -20°C to +180°C / PVDF: -20°C to +120°C |
|
Fluid Temperature (Alloy)
|
SS316: -20°C to +150°C / Duplex: -20°C to +230°C / Hastelloy: -20°C to +260°C |
|
pH Range
|
0 to 14 (full range with appropriate material) |
|
Motor Power Range
|
0.75 kW to 110 kW (1 to 150 HP) |
|
Voltage Options
|
230V / 400V / 415V / 460V / 690V |
|
Speed
|
1,450 / 2,900 RPM (50Hz); 1,750 / 3,500 RPM (60Hz) |
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Port Size
|
25 mm to 250 mm (1" to 10") |
|
Alloy Materials
|
SS304 / SS316 / SS316L / Duplex 2205 / Super Duplex 2507 / Hastelloy C276 / Titanium Gr2 / Zirconium |
|
Shaft Sealing
|
Double mechanical seals (API 682) / Magnetic drive (sealless) / Single mechanical seal (non-hazardous) |
|
Design Standard
|
ISO 5199 / ISO 2858 / EN 22858 / API 685 (magnetic drive) |
Six key engineering benefits that make our acid and alkali resistant pump the preferred choice for corrosive chemical transfer.
We do not offer a one-size-fits-all solution. Our material selection process matches the alloy or lining to your specific chemical, concentration, temperature, and impurities. We provide detailed material compatibility charts and work with you to select the optimal material for longest service life.
For toxic, carcinogenic, or environmentally hazardous chemicals, we offer double mechanical seals with barrier fluid (API 682 Arrangement 2 or 3) and magnetic drive (sealless) pumps. Magnetic drive pumps provide absolute zero leakage to the atmosphere, eliminating emissions and enhancing worker safety.
Our alloy pumps handle aggressive chemicals up to 260°C (Hastelloy) and our PFA-lined pumps handle chemicals up to 180°C. This capability is essential for hot acid transfer, concentrated caustic at high temperature, and many chemical processes where cooling is not possible.
CFD-optimized impeller and volute designs achieve efficiencies up to 82 percent at best efficiency point for lined pumps, and up to 88 percent for alloy pumps. Lower power consumption reduces operating costs and carbon footprint.
Back pull-out design allows removal of the rotating assembly (impeller, shaft, bearing housing, mechanical seal) without disconnecting pump casing from piping. For lined pumps, we provide spacer couplings to allow seal replacement without disturbing motor alignment.
Every alloy component is traceable to its heat number with chemical composition and mechanical properties documented on EN 10204 3.1 or 3.2 certificates. Positive Material Identification (PMI) is performed on every alloy pump component before shipment.
Trusted across chemical processing, metal finishing, and water treatment for corrosive fluid handling.
A detailed comparison of corrosion resistant materials for acid and alkali service.
| Material | Best Chemical Resistance | Limitations | Max Temp | Relative Cost |
|---|---|---|---|---|
| PTFE Lined | Virtually all chemicals except molten alkali | Limited mechanical strength | >120°C (PTFE) / 180°C (PFA) | >2.0x |
| SS316 | Dilute acids, alkalis, organic solvents | Poor in chlorides, reducing acids (HCl, HF) | >150°C | >1.3x |
| Duplex 2205 | Chlorides, brackish water, mild acids | Limited in highly reducing acids | >230°C | >2.2x |
| Hastelloy C276 | Wet chlorine, HCl, HF, mixed acids | Less effective in oxidizing conditions | >260°C | >5.5x |
| Titanium Gr2 | Seawater, wet chlorine, oxidizing acids | Not for dry chlorine, reducing acids | >230°C | >8.0x |
| PVDF Lined | Acids, alkalis, solvents (economical) | Lower temperature limit than PTFE | >120°C | >1.5x |
Maximize the corrosion resistance, safety, and service life of your acid and alkali resistant pump.
Even small changes in concentration, temperature, or impurities can dramatically affect chemical compatibility. Always consult the material compatibility chart for your specific chemical, concentration, and operating temperature before selecting materials. When in doubt, choose a higher-grade material for safety.
Running a chemical pump dry will quickly destroy the mechanical seals. For lined pumps, dry running can also damage the PTFE liner. Install low level protection devices on your tank or sump. For double mechanical seals, maintain barrier fluid pressure at all times.
For PTFE and PFA lined pumps: before extended shutdowns of more than 2 weeks, flush the pump with a neutral liquid (water or compatible solvent). Some chemicals can permeate the fluoropolymer lining over time; flushing removes the chemical and prevents permeation-blistering or swelling of the lining.
For double mechanical seals with pressurized barrier fluid (API Plan 53), monitor the barrier fluid reservoir level and pressure daily. A drop in level indicates the inner seal is leaking into the pump. A drop in pressure indicates the outer seal is leaking. Prompt maintenance prevents cross-contamination and environmental release.
Excessive piping loads can distort the pump casing, causing misalignment, seal failure, and reduced efficiency. This is especially critical for lined pumps, where the PTFE liner can be damaged by casing distortion. Install independent pipe supports near the pump flanges.
For Hastelloy, titanium, and duplex pumps, perform Positive Material Identification (PMI) testing on the pump casing and impeller before installation. This verifies that the correct alloy was supplied. Visual inspection cannot distinguish between SS316 and Hastelloy. We provide PMI certificates with every alloy pump.
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