SMT-FB Series Oil-Water Separators

A standardized oil-water separation solution for individual tanks and independent circulation systems. It continuously removes floating surface oil and promotes the coalescence and rise of separable dispersed oil droplets, while the V-shaped bottom collects and discharges settled solids.

Oil-Water Separation for Individual Tanks with Centralized V-Bottom Sludge Discharge

The FRIESS SMT-FB Series combines floating surface suction with physical coalescence separation. The floating intake continuously recovers oil-bearing liquid near the surface. Fine, coalescible dispersed oil droplets attach to the oleophilic polypropylene media, collide and merge, then rise for separation. A V-shaped bottom collects settled solids for periodic discharge.

Seven standard flow rates from 450 to 11,300 L/h cover machine-tool tanks, industrial washing tanks and independent circulation systems. Model selection should consider fluid properties, oil loading, target circulation rate, daily operating time and settled-solids loading. For higher capacity, centralized supply, multiple tanks or multiple suction points, choose the SMT-FL Series oil-water separator.

FRIESS SMT-FB industrial oil-water separator for continuous tramp-oil removal from process fluids
450–11,300 L/hStandard Processing Flow Rate
Seven Standard ModelsCovering Different Circulation Requirements
V-Shaped Tank BottomCollects and Discharges Settled Solids
304 Stainless SteelIndustrial Separation Tank

On-Site Product Photos

SMT-FB oil-water separator installation diagram showing floating suction, pumping, separation, waste-oil discharge and clean-liquid return

How the SMT-FB Works

The floating suction device follows changes in liquid level, keeping the intake close to the surface. Oil-bearing liquid is continuously recovered and pumped to the SMT-FB separation tank. Fine, coalescible droplets attach to and merge on the oleophilic media, then rise after forming larger droplets; settled solids collect at the V-shaped bottom for periodic discharge.

Floating-Oil Recovery Performance

On-Site Comparison with a Floating Suction Device

This installation uses a floating surface suction device. The intake follows changes in liquid level, remains near the surface and continuously transfers oil-bearing liquid to the SMT-FB separation tank for subsequent coalescence separation.

Before Operation

Floating oil visible before operation of the FRIESS SMT-FB floating suction device
Significant Floating Oil Visible at the Surface

After Continuous Operation

Floating suction unit collecting surface oil from a milky process liquid
Visible Floating Oil Substantially Reduced

SMT-FB Series Models and Technical Specifications

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ModelStandard Flow Rate (L/h)Dimensions (L × W × H, mm)Separation Tank Material
SMT450-FB450838 × 415 × 1066304 Stainless Steel
SMT680-FB680991 × 415 × 1066304 Stainless Steel
SMT1100-FB11001219 × 415 × 1066304 Stainless Steel
SMT2200-FB22001219 × 720 × 1066304 Stainless Steel
SMT3400-FB34001219 × 1024 × 1066304 Stainless Steel
SMT5600-FB56001524 × 1330 × 1066304 Stainless Steel
SMT11300-FB113001829 × 1024 × 1676304 Stainless Steel

Custom specifications are available for specific operating conditions.

Inside a FRIESS SMT-FB oil-water separator showing collected oil above the cleaned-fluid return area

SMT-FB oil-water separation in operation | Top: the separated oil phase rises and collects at the surface; bottom: return zone for the treated liquid. Actual separation conditions depend on fluid properties, oil loading and operating conditions.

MODEL SELECTION

How to Select the Right SMT-FB Model

SMT-FB model selection should not be based on tank volume alone. Fluid properties, oil loading, target circulation rate, daily operating time and settled-solids loading must also be considered.

Information Required for Model Selection

Capacity and On-Site Configuration

The standard SMT-FB Series offers seven flow rates from 450 to 11,300 L/h. Higher capacities, special connections and special site conditions can be accommodated through application-specific configurations.

SEPARATION IN ACTION

Coalescence Separation in Operation

The video shows the SMT-FB separation tank in actual operation. The separated oil phase collects at the surface while the treated liquid enters the return zone.

Note: The video reflects operation under specific site conditions. Actual results depend on fluid properties, oil loading and operating conditions.

Inside the SMT-FB Separation Tank | 45-Second Video
COALESCING PRINCIPLE

Why Must Fine Oil Droplets Coalesce and Grow in the SMT-FB?

The SMT-FB separation tank contains oleophilic polypropylene coalescing media with a specific surface area of approximately 433 m²/m³. Fine, coalescible dispersed droplets attach, collide and merge on the media as they pass through it. As the droplets grow, their rise velocity increases, allowing them to collect at the surface and be discharged more readily.

Theoretical Rise Times for Different Oil-Droplet Diameters

Time Required for Oil Droplets to Rise 75 mm (3 in)
Droplet Diameter (μm)Rise Time
30012 sec
15042 sec
604 min 12 sec
3017 min 24 sec
151 h 8 min 54 sec
510 h 2 min 9 sec

Note: The table shows theoretical values calculated under specified assumptions. Actual separation time varies with fluid properties and operating conditions.

Why Do Larger Oil Droplets Rise Faster?

According to Stokes’ law, under ideal conditions such as low Reynolds number and approximately spherical droplets, the theoretical terminal rise velocity is proportional to the square of the droplet radius:

Stokes law chart showing the relationship between oil-droplet diameter and rise velocity

V: terminal rise velocity; g: gravitational acceleration; r: droplet radius; Δρ: density difference between the continuous liquid phase and the oil droplet; μ: dynamic viscosity of the continuous liquid phase.

When other conditions are unchanged and the assumptions apply, doubling the droplet radius increases the theoretical rise velocity by approximately four times.

Note: Actual separation performance is also affected by liquid viscosity, temperature, density difference, droplet shape and flow conditions.

FAQ

SMT-FB Frequently Asked Questions

How Does the SMT-FB Differ from a Conventional Oil Skimmer?

A conventional oil skimmer mainly recovers floating oil that has already formed a layer at the surface. The SMT-FB uses floating suction to recover oil-bearing surface liquid and coalescing media to help fine dispersed droplets merge and rise. It therefore removes floating oil and reduces the concentration of coalescible dispersed droplets. Its V-shaped bottom also collects and discharges settled solids.

Can the SMT-FB Remove Oil from Emulsions?

The SMT-FB primarily removes floating oil, free oil and coalescible dispersed oil droplets from emulsions. The physical separation process does not actively break the chemical structure of emulsifiers. Chemically stable emulsified or dissolved oils may respond differently depending on the formulation, droplet size and operating conditions; testing with a fluid sample is recommended.

Does Installing the SMT-FB Require Tank Modifications?

Major tank modifications are normally unnecessary. The unit can be installed beside the tank and connected to the existing system through the floating suction device, transfer piping and return piping. Connections, piping, power supply and equipment position can be configured for the available space and tank design.

Does the Coalescing Media Require Periodic Replacement?

There is no universal replacement interval for the coalescing media. Maintenance frequency depends on fluid type, oil loading, solid contamination and operating time. If flow rate declines, separation performance changes or the media becomes visibly contaminated, inspect, clean or replace it according to the maintenance requirements.

Can Liquid Treated by the SMT-FB Be Discharged Directly?

Not necessarily. The SMT-FB removes free oil, floating surface oil and coalescible dispersed oil droplets; it is not a complete industrial wastewater treatment system. Where specific discharge limits apply, downstream treatment must be selected for the water quality, contaminant composition and local requirements, and compliance must be confirmed by testing.

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