| End-Suction Centrifugal Pump | A rotating impeller converts motor energy into fluid velocity and pressure. | 10–1,500 m³/h | 1–10 bar | Approximately 1–500 cSt; efficiency decreases as viscosity rises. | Usually no; requires a flooded suction or a priming system. | Low tolerance. Clean or lightly filtered oil is recommended. | High-volume transfer of low- to medium-viscosity diesel, fuel oil, crude oil, and lubricating oil where the storage tank is close to the pump. | High flow capacity, simple construction, smooth delivery, and generally low initial cost. | Performance is sensitive to suction conditions and oil viscosity. Cavitation can occur if NPSH is insufficient. |
| Positive-Displacement Gear Pump | Meshing gears trap and move a nearly fixed volume of liquid per revolution. | 0.1–200 m³/h | 2–25 bar | Approximately 10–100,000 cSt, depending on clearance, speed, and heating. | Generally yes, when correctly specified and operated within the manufacturer's limits. | Limited tolerance. Abrasive particles can accelerate gear and casing wear. | Metered or controlled offloading of lubricating oil, heavy fuel oil, bitumen-related fluids, and other viscous products. | Good suction lift, accurate displacement, compact size, and relatively stable flow at changing discharge pressure. | Requires a relief valve or bypass protection. Excessive speed may cause slip, heat generation, or cavitation. |
| Twin-Screw Pump | Two synchronized screws transport liquid axially through the pump casing. | 5–1,000 m³/h | 2–40 bar | Approximately 1–1,000,000 cSt, subject to product temperature and pump design. | Yes, commonly suitable for suction-lift service. | Moderate to good tolerance for small quantities of soft solids or entrained gas; abrasive solids still require filtration. | Ship, tanker-truck, railcar, and terminal offloading where products vary in viscosity or may contain entrained air. | Handles a broad viscosity range, provides low-pulsation flow, and can often operate in both transfer directions. | Higher purchase price and more demanding timing, lubrication, and maintenance requirements than basic centrifugal pumps. |
| Progressive Cavity Pump | A rotating helical rotor moves sealed cavities through a flexible stator. | 0.1–150 m³/h | 2–30 bar | Approximately 100–1,000,000 cSt, depending on speed and elastomer selection. | Yes, with strong suction capability when properly installed. | Good tolerance for suspended soft solids and some contaminated fluids. | Heavy crude, waste oil, emulsified oil, sludgy oil mixtures, and products that require gentle handling. | Low-pulsation transfer, good suction performance, and suitability for high-viscosity or non-uniform liquids. | The stator can be damaged by dry running, excessive temperature, incompatible chemicals, or abrasive solids. |
| Rotary Vane Pump | Sliding vanes create expanding and contracting chambers that draw in and discharge liquid. | 5–150 m³/h | 1–10 bar | Approximately 1–10,000 cSt, depending on vane material and operating speed. | Yes; commonly used where suction lift is required. | Low to moderate tolerance. Clean fluid and effective filtration improve service life. | Truck loading and unloading, mobile oil transfer skids, and medium-flow handling of diesel, fuel oil, and lubricants. | Good self-priming, compact design, reversible operation on suitable models, and reliable flow control. | Vanes are wear components. Dry running, abrasive contamination, and excessive speed can shorten operating life. |
| Air-Operated Double-Diaphragm Pump | Compressed air alternately flexes two diaphragms to displace liquid through check valves. | 0.1–60 m³/h | Up to approximately 8 bar | Approximately 1–50,000 cSt, depending on diaphragm material and flow rate. | Yes, generally capable of dry lifting and intermittent service. | Good tolerance for contaminated liquids and some suspended solids, subject to valve clearance. | Intermittent offloading, emergency transfer, drum and tote emptying, and hazardous areas where electric motors are restricted. | Can run dry for limited periods, offers no electrical motor at the pump, and provides strong containment flexibility. | Pulsating flow, compressed-air consumption, higher noise, and lower energy efficiency for continuous high-volume transfer. |
| Submersible Centrifugal Pump | A motor-driven impeller operates while the pump is immersed in the tank, pit, or vessel. | 10–1,000 m³/h | 1–8 bar | Approximately 1–300 cSt for standard designs; high-viscosity service requires special selection. | Not applicable; the pump is installed below the liquid surface. | Low to moderate tolerance, depending on impeller clearance and filtration. | Bottom unloading from storage tanks, collection pits, barges, and vessels where suction piping must be minimized. | Reduced priming problems, short suction path, low risk of suction-line air leakage, and efficient high-flow transfer. | Access for maintenance can be more difficult. Motor cooling, cable sealing, hazardous-area certification, and tank compatibility must be checked. |