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Pulsation Dampener, SS/Viton

Additional Information

SKU 110-065
Price
$1,034.23
Name Pulsation Dampener, SS/Viton

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Pulsation Dampener, SS/Viton
Pulsation Dampener, SS/Viton

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Pulsation Dampener, SS/Viton

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Applications: 

Chemical Processing

  • Organic Concentration, Fractionations and Purification
  • Chemical Fractionation
  • Valuable Metal Reclamation

Biomedical

  • Enzyme Purification
  • Protein Separation and Concentration
  • Plasma Separation
  • Cell Harvesting

Membrane Studies

  • Chemical Compatibility
  • Cleaning Procedure Efficacy
  • Slip-Stream Monitoring of Larger Membrane Systems
  • Scale-Up Studies

Operation:

  • Accepts Any Flat Sheet Membrane: Maximum flexibility ensures the most efficient and cost effective membrane is chosen for future scale-up or small scale production. Sepa CF II Membrane Cell System accommodates any 19 cm x 14 cm (7.5 in x 5.5 in) flat sheet membrane for a full 140 square cm (22 square inches) of effective membrane area. For convenience, Sterlitech offers precut and individually wrapped membrane inserts in single packs from our large selection of reverse osmosis (RO), Nanofiltration (NF), ultrafiltration (UF), and microfiltration (MF) membranes. Some assortment packs are available. 
  • Unique Piston Clamping Mechanism: Membrane change out takes less than one minute. The unique patented mechanism quickly seals the cell and provides uniform pressure to assure a perfect seal – a significant improvement over other multiple bolt lab scale units with inherent, uneven torque and leak problems. Sepa CF II Membrane Cell System’s versatile hydraulic mechanism utilizes a hand pump for its pressure sources. The pressure relief valve is set to 1,000 psi. We strongly recommend the hand pump as a safety feature. 
  • Compatible With Wide Range of Feed Flow Fluid Pumps: Special pumps are not required. Many standard lab scale pumps can provide the wide range of pressure and flow that the Sepa CF II Membrane Cell System is capable of using. Any pump operating less then 2 gpm should work with the system. We recommend a piston driven diaphragm pump. 
  • Concentrate Flow Control Valve: Stainless steel concentrate flow control valve gives users accurate control of pressure and flow over the membrane surface. This easy-to-use valve is mounted on the concentrate outlet of the cell and is easily removed for inspection and cleaning. 
  • Stainless Steel Cell With Viton®* O-Ring: The 34 mil or 75 mil stainless steel cell body contributes to flexibility of use by allowing almost any type of substance through the membrane cell. 
  • Wide Variety of Feed Spacers and Permeate Carriers: User selects from a variety of spacer configurations, identical to those used in large-scale sepralators, to help optimize flow characteristics for the particular solution being processed. Mesh or tubular feed spacers (along with the membrane and the permeate carrier) are loaded in the stainless steel cell body to simulate the actual flow of characteristics of a wide variety of available spiral-wound and tubular membrane elements. These spacers, in conjunction with the concentrate flow control valve, allow the user to test laminar or turbulent flow conditions. 
  • Wide Variety of Shims and Spacers: Optimizes flow characteristics during filtration, maximizing membrane efficiency. Placing the correct shim and spacer to fill the cell cavity when used with the membrane and permeate carrier may optimize flow conditions. Suggested 1-2 mil of space should remain after the complementary shim and spacer are selected. We strongly recommend when using thinner feed spacers the use of the complementary shim to allow the system to properly work. 
  • Multiple Ports for Instrumentation: Pressure gauges, flow meters, pH monitors, etc., are easily connected to the cell to monitor important process parameters. Pressure gauges indicating piston sealing pressure and concentrate fluid pressure are included as standard features with the system. 
  • Laminar or Turbulent Flow: Shear sensitive feed solutions can be processed in laminar flow mode while less sensitive solutions can be processed in turbulent flow mode to lessen membrane fouling. Sepa CF II Membrane Cell System is versatile enough to operate in either flow mode.  
  • Pressures to 1,000 psi (69 bar): Separations can be performed at optimum rates, thus saving time and money. Permeate flow rate is approximately proportional to driving pressure. Therefore, higher pressure means higher permeate flow and faster concentrations. Lower pressures can be used to satisfy special membrane or solution requirements.
Sepa CF Flow Diagram  PDF
Sepa CF Operation Manual PDF
Sepa CF Systems Principles of Operation PDF
Hydracell Pump Options PDF
 
Specification Description
Data applicable for Sepa CF
Effective Membrane Area 140 cm² (22-inch²)
Hold-Up Volume 70 ml (2.4 ounces)
Maximum Pressure (316SS Cell Body) 69 bar (1000 psig)
Maximum Temperature (316SS Cell Body) 177°C (350°F)
O-rings Viton* (Other materials available)
pH Range Membrane Dependent
Cross Flow Velocity Variable - See Table 2.1 in the Sepa Manual

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.

How is the Sepa System repassivated?

Q. How is the Sepa System repassivated?

A. Passivation is a process that will remove free iron deposits and will add future protection to your Sepa System. To passivate the Sepa System, swab the entire unit with either a 20% Nitric Acid (1st choice) or Phosphoric Acid (2nd choice) solution. Make sure to use good Nitric Acid or Phosphoric Acid handling precautions such as gloves, eye goggles, etc. when performing passivation. Rinse unit off with conditioned water such as distilled.

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.