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CF042 Crossflow Cell

CF042 Crossflow Cell
The Sterlitech CF042 membrane cell is a lab scale cross flow filtration unit designed to provide fast and accurate performance data with minimal amounts of product, expense, and time.

Please note: A feed flow pump is required to operate the CF042 cross flow cell unit. We recommend the Hydracell pump by Wanner Engineering, which is a positive displacement, diaphragm pump designed for high pressure, lower flow applications. When ordering, be sure to specify the power requirements for the motor. The minimum power available is 110V, 60 Hz. 220 V and 50 Hz motors are also available. There may be an additional cost if a variable speed drive is required.

To discuss these options further and to receive a more detailed price quote on a new CF042 membrane cell unit, contact us at 1-877-544-4420 or sales@sterlitech.com.

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SKU Material Type Name Price  
CF042 Delrin Acetal Cell CF042 Crossflow Cell
$811.13

M03SASGSNSCA M-03S Hydracell Pump (110 or 220V/1ph)
$3,083.08

M03SASGSNSCA-V M-03S Hydracell Pump (220V/3ph for variable speed)
$3,083.08

1149420 Pressure Gauge with "T" Fitting (3/8" Tube Fittings)
$122.50

1149421 Needle Valve with "T" Fitting (3/8" Tube Fittings)
$149.95

F-55376L Site Read Flow Meter, 0.2 to 2 GPM
$135.00

CF042P PTFE Cell CF042 Teflon Crossflow Cell
$838.16

CF042SS316 316 SS CF042 Stainless Steel Crossflow Cell
$3,038.50

CF042AC Acrylic CF042 Acrylic Crossflow Cell
$838.16

1149423 N/A Pressure Relief Valve (1000 PSI/69 bar) for CF Feed Flow Pump
$325.00

1149424 N/A Pressure Relief Valve (350 PSI/24 bar) for CF Feed Flow Pump
$325.00

1230066 N/A Conical Feed Tank, 1.5 Gallon Stainless Steel, with 'T" fitting
$1,129.00

1230067 N/A Conical Feed Tank, 5.0 Gallon Stainless Steel, with 'T" fitting
$1,556.00

13 Item(s)

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  • Bench scale membrane development
  • Purifying Fluids

CF042 Manual  PDF

CF042 Flow Diagram  PDF

Specification Description
Active Membrane Area 42 cm²
Maximum Pressure 1000 psig (69 bar) (400 psi for PTFE version)
Maximum Temperature 180°F (80°C)
Connections Feed: ¼” FNPT (base of cell) ; Concentrate: ¼” FNPT (base of cell) ; Filtrate: 1/8” FNPT
Cell Body Acetal, Acrylic, PTFE, or Stainless Steel
"O" - Ring Buna-N (Viton availble upon request)
Outer Dimensions 5” X 4”x 3¼” (12.7cm x 10cm x 8.3 cm)
Active Area Dimensions 3.625” x 1.800"(9.207 cm x 4.572 cm)
Slot depth 0.09” (0.23 cm)
Support Membrane 20 micron sintered stainless steel
Torque Settings for Coupling Delrin: 60 inch-pounds ; Acrylic: 70 inch-pounds ; PTFE: 15 inch-pounds

What is the difference between Sepa CF and Sterlitech HP4750?

Q. What is the difference between Sepa CF and Sterlitech HP4750?

A. The Sterlitech HP4750 is an enclosed batch system (limited to 300ml) with direct filtration under pressure. There is a stir bar mixing the solution and pressures up to 1000 psi may be applied.

The Sepa CF is a crossflow system that allows continuous sampling and testing under different pressure and flow rate parameters depending on the pump and fluid.

Does the feed spacer penetrate the membrane?

Q. Does the feed spacer penetrate the membrane?

A. The mesh spacer usually leaves an imprint on the membrane which is not a problem - unless too thick of a mesh is used - then it could damage the membrane.

How do I calculate Reynolds number based on the feed cross-flow velocities for the various feed spacers?

Q. How do I calculate Reynolds number based on the feed cross-flow velocities for the various feed spacers?

A. The Sepa CF cell for use with high fouling spacer has a flow area width and height of 3.7 inches by 0.068 inches. Once a spacer material is placed in the channel the actual flow channel cross section is significantly reduced. We have not calculated that. We typically operate the cell and estimate the Reynolds number at the transition from laminar to turbulent flow by monitoring the increase in pressure drop as the crossflow is increased.

Another usage implementation which we have used is the placement of a rubber gasket in the flow channel. A specifically sized flow channel can be cut out of the gasket to define a flow channel of the desired cross section.

We actually have done more study of the CF cell for use with standard spacer (3.7 in. by 0.034 in. cell cross-section). We evaluated that cell for various cross flow velocities at various feed flow rates.

How do I distinguish between the low foulant (34ml) feed spacer and the high foulant (68ml) feed spacer when I hold them in my hands?

Q. How do I distinguish between the low foulant (34ml) feed spacer and the high foulant (68ml) feed spacer when I hold them in my hands?

A. The low foulant has smaller squares and bends slightly easier.  It feels lighter.  It is not stiff like the medium foulant.  The high foulant spacer has corragated ridges in it like cardboard.  No holes.

Is the low foulant spacer the same as the permeate carrier?

Q. Is the low foulant spacer the same as the permeate carrier?

A. No, the low foulant spacer is under the membrane and the permeate carrier is on top. The membrane is sandwiched between the spacer and permeate carrier.

In the instruction manual of the Sepa CF, tubular and mesh spacers are mentioned. Can I conclude that the tubular is the low foulant and the mesh is the high foulant?

Q. In the instruction manual of the Sepa CF, tubular and mesh spacers are mentioned. Can I conclude that the tubular is the low foulant and the mesh is the high foulant?

A. The mesh spacer is a low (34 ml) and also the medium spacer (68 ml).

The tubular spacer is for high foulants (68 ml) and looks like corregated cardboard.

Could the filter cloth of industrial filters be used in the Sepa filtrations units, after cutting it to proper size?

Q. Could the filter cloth of industrial filters be used in the Sepa filtrations units, after cutting it to proper size?

A. The Sepa CF can potentially work for any media that can be fitted into the chamber.

One thing that could be an issue for some types of filter media is whether or not a sufficient seal is made between the O-ring and the media. For membranes, this is not a problem because membranes have a relatively smooth surface, which affords good mechanical seal when pressed together. A large fiber woven material, for example, may need to be modified or filled with some type of potting compound to level the surface in order to get a non-bypass seal.

Can I use the Sepa CF membrane cell without spacers?

Q. Can I use the Sepa CF membrane cell without spacers?

A. Using the cell without any spacers will usually cause wrinkles in the membrane. The depth of the cell is made to accommodate the spacer that will fit in it (34 or 68 ml).

How can I set the maximum flow from my Sepa CF?

Q. How can I set the maximum flow from my Sepa CF?

A. Most separations and flux through membranes are controlled by the nature of the fluid. For salt rejecting membranes, such as RO and NF, the dominant variables are operating pressure and osmotic pressure (a solute concentration-dependent property which reduces net operating pressure with increased solute concentrate).

The pumping rate or fluid velocity across the membrane is another important operating parameter; an increased velocity results in improved mixing of the layer of feed solution directly above the membrane. The removal of fluid through the membrane results in accumulation of rejected solutes in this layer, often referred to as the boundary layer. The boundary layer can contribute a significant resistance to flux through the membrane as levels of solutes increase.

The accumulation of solutes in the boundary layer is often the most limiting factor in membrane flux, particularily for the larger pored membranes (NF, UF, and MF). There generally is a finite operating pressure, above which provides little or no flux benefit.

An increase in the feed solution velocity across the membrane, combined with turbulence promoting mesh spacers, can provide the optimal combination of operating conditions. Consideration of energy imput and mechanical load due to pressure drop across the membrane are practical limitations for operation of membrane systems.

To find maximum flux, we set the feed flow to a maximum practical rate, and increase the operating pressure incrementally while monitoring flux (filtrate) output. A given operating pressure will yield a certain maximum output for a specific feed solution.

If the feed solution becomes more concentrated, such as occurs for a dewatering objective, the optimal operating pressure will typically decrease as the solute concentration increases (the exception to this would be if the osmotic pressure increase due to concentration becomes significant). The input energy may be better applied to higher cross flow velocity if practical.

A practical method may include operation at a pressure setting slightly lower than the maximum initial rate determined. This is produce highest flow, best flux, and least amount of build up on membrane.

What is the definition of GFD?

Q. What is the definition of GFD?

A. GFD = Gallons Per Square Foot of Membrane Per Day

Will there be a difference in flow rate on the Sepa CF if it is run continuously or in intervals?

Q. Will there be a difference in flow rate on the Sepa CF if it is run continuously or in intervals?

A. If permeate flow rate verses time for both membranes are plotted will there be a difference?

There should be a difference in the plots - at least initially. There is typically a "conditioning" affect that occurs as the result of mechanical compression, some of this affect is reversible to an observable amount if operation is intermittent.

This will yield a "zigzag" appearance to a graph of operation vs. time or cumulative hours of operation. The trend with the intermittent operation would be to gradually approach a standard.

What fluid do I use in my Hydraulic hand pump for my Sepa CF?

Q. What fluid do I use in my Hydraulic hand pump for my Sepa CF?

A. The unit uses standard grade hydraulic oil. It has a reservoir located under the handle at the furthest end with a cap on the reservoir.

The amount of oil used will depend on the length of line, hose.

The recommended oil has a viscosity rating at 100°F.

SUS rating 150-165

SAE 10 wt oil Hydraulic oil (do not use other types of oils)

General purpose

150-165 thickness

Rating 210°F 42-45

What is the proper way to store the membranes for the Sepa CF after they have been used?

Q. What is the proper way to store the membranes for the Sepa CF after they have been used?

A. We recommend that the membranes for the Sepa CF be kept wet once used. Either keep the water fresh (change every couple of days), or add ~0.5 sodium metabisulfite (preferred) to keep bacteria from growing.

What are the torque settings for the CF042 and Sepa CF Cells?

Q: What are the torque settings for the CF042 and Sepa CF Cells?

A: Best practices for plumbing of polymer (Acrylic, Delrin, and PTFE cells) CF042 cells, include the use of Teflon tape properly installed on 1/4npt threaded coupling, and the use of a light coat of Teflon based pipe thread sealant, then the coupling needs to be seated in the base of the cell using the following torque settings:

  • Delrin- 60 inch pounds
  • Acrylic -70 inch pounds
  • PTFE -15 inch pounds OR until the fitting "shoulders" out on the base of the CF042 cell*

*extreme caution should be used to assure that the fitting is not started incorrectly (cross-threaded).  In normal installation, the fitting should easily turn in several turns without tooling (by "hand") before using the torque wrench.