Designed for efficient solid/liquid separation, recessed chamber filter presses and filter plates are popular in a wide array of industries, from industrial and municipal wastewater to chemical processing. Learn how these types of filter presses and plates work and their advantages. Then, reach out to a member of our Sales and Service Team here at M.W. Watermark' to see if a recessed chamber filter press is right for your application.
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Like all filter presses, recessed chamber filter presses work by using a pressure filtration system. They have filter plates that hang on a steel frame. These plates ' usually made from polypropylene ' come in gasketed and non-gasketed designs.
Gasketed filter plates help eliminate leaks, while non-gasketed filter plates make filter cloth installation faster since the cloths do not need to be pounded in but may result in a bit of leakage. Regardless of which type is utilized, the filter plates are clamped together in a filter press using a hydraulic cylinder and pump. Since each plate features a recessed area, when the plates are pushed together, they form a chamber in which solids collect on the filter cloths.
During the filtration process, slurry is usually fed through a large center feed hole. Liquids will pass through the filter cloth and onto the drainage surface. The liquids will eventually make their way through the discharge piping and into a process tank or drain. Meanwhile, the solids will accumulate on the filter cloths in the cavity that was formed when the plates were clamped together. Depending on the nature of the slurry, recessed chamber filter presses and plates can produce filter cakes consisting of 20 to 85 percent solids.
Click below to watch our introductory video, which illustrates the role of filter plates, filter cloths and pressure filtration in forming a dewatered filter press cake in a recessed chamber filter press.
Recessed chamber filter presses and plates are used in various industries to effectively separate liquids and solids. Some common industrial applications for this type of filter press include:
One of the top benefits recessed chamber filter presses have to offer involves how they are fed. With a large feed hole in the center of the plate stack, the slurry is able to fill the cavities swiftly and more evenly. This helps rule out the possibility of clogging and blowing out, helping prolong the life of your plates. This is especially important in applications with high feed solids.
A second advantage comes courtesy of the plates they utilize. As previously mentioned, recessed filter plates are available in both gasketed and non-gasketed versions ' and even in non-gasketed plates, there is an option for the addition of latex that runs along the edge of the filter cloth to help minimize wicking. No matter which type of recessed chamber filter plate works best for your particular application, liquids can generally be contained with proper operation.
Finally, recessed chamber filter plates make it relatively easy to empty the filter cakes. When the press is opened and the plates are shifted, the filter cakes will typically fall out from the chambers into a cake hopper or drum for simple removal. If the cakes remain in place, minor manipulation from a spatula will usually release them.
Interested in taking a deeper dive into how recessed chamber filter presses are designed and how they work? Learn more.
M.W. Watermark offers both stock and customized recessed chamber filter presses to accommodate your exact specifications. If you are in need of a recessed chamber filter press, replacement recessed chamber filter plates or other aftermarket parts and retrofits, contact us today.
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Plate and frame filter presses have been used for many years, and predate the recessed chamber filter press, which is the type that most people think of today when they hear the term 'filter press'. Although recessed chamber presses are now more of the norm, the plate and frame design has some advantages with certain applications and is still used today.
The plate and frame design utilizes a flat, solid plate (known as a 'flush plate') covered by a filter press cloth, with a hollow frame between each plate. A metal skeleton holds and clamps the filter plates together to create a chamber, which is formed by the flush plate on each side of a frame. Filter cake is collected within the frame. Historically, plates were made of wood or cast iron. Today, the most common material is polypropylene.
The slurry is pumped into a corner hole and flows into each frame, allowing solid particles to accumulate on the filter cloths. The remaining filtered liquid (also known as filtrate) then moves to a drainage port in the flush plate and into a corner hole that is not being used for feeding the slurry. The filtrate then travels to discharge piping and is directed to the next step in the process.
After a period of time, the frames become filled with solids, the slurry feed pump turns off, and the filter press is ready to open. Each frame should now contain a filter cake, which is the end result of the solids forming on the filter cloths. The filter cakes are then scraped out of the frames using a spatula, ideally falling into a cake hopper placed below the press.
The primary advantages of plate and frame presses are the ability to quickly change the filter cloths as well as the ability to use a wider range of materials for the filtration medium, including paper, which is often used for fine filtration applications.
For example, in a process where immediate particle retention is important, filter paper may be required as fine solids would either blind off the filter cloth or simply pass through it. Note that filter cloths are still in place to support the filter paper. The filter cloths are reused, but the filter paper is replaced after every filtration cycle.
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Plate and frame presses are best suited for projects where filtration area is more important than volume. This is why plates and frames have their greatest prominence in polishing applications (as opposed to dewatering projects), where the feed solids concentration is often well below 1% by weight.
Polishing applications are sized for a particular filtration area based on the process flow rate and the known flux rate (volume per area per unit of time). To avoid dips in achievable filtration flow as the press fills with solids, polishing applications usually include a redundant filter press that is also sized to accept 100% of the desired process flow.
One disadvantage of the plate and frame design is the potential for building uneven pressure between frames, which can lead to plate damage. This issue stems from the fact that the frame is being fed through a small opening in the corner, which can lead to blockage. This clogging can cause one frame to become full while the next frame in-line remains empty.
Another disadvantage is the potential for leakage. The filter plates used in plate and frame presses are non-gasketed, which allows them to wick liquid under pressure. This type of filter press is usually mounted on a raised platform or positioned over a pit where any leaked liquids can be collected more conveniently.
A recessed chamber filter press utilizes filter plates that form a series of cavities between them when they are clamped together. Suspended particulates collect on the filter cloths and build up inside each cavity space to form a filter cake. Compare this to the hollow frames of the plate and frame design where solids are collected.
The skeleton of a recessed chamber filter press is constructed in a similar fashion as a plate and frame press where the plates hang on a steel frame, and the frame acts as a clamping device for the filter plates. Both types of presses also utilize a hydraulic cylinder and pump for opening, closing, and clamping the press.
As with plate and frame filter plates, recessed chamber plates are most commonly made from polypropylene. However, recessed chamber plates can be either gasketed or non-gasketed. Gasketed plates offer greater protection from leakage, but can also require a more time-intensive cloth changing process. Non-gasketed cloths or plate and frame cloths can have latex applied to the edges to help minimize (but not eliminate) wicking.
Slurry is pumped into the filter press through the feed (most commonly in the center of the plate) and the solids are distributed evenly in each chamber throughout the press (1). Solids begin to build on the filter cloths. Most of the solid/liquid separation is accomplished by the particulates building on the cloths. At first, some fines pass through, but eventually the solids begin to form a layer on the cloths (2). This layer traps the fine particles and eventually forms a filter cake. The filter cake then serves as a depth filter as the dewatering process continues.
The filtrate (liquid) usually exits the filter pack (plates) through corner ports into a manifold. When the correct valves in the manifold are open, the filtrate exits the press through a single point, the filtrate outlet. The filtrate is then directed via discharge piping to the next step in the process.
As the filter press builds pressure, the solids build within the chambers until they are completely full of filter cake (3). Once the chambers are full, the fill cycle is complete, and the filter press is ready to be emptied (4). The press is then opened, and the plates are moved apart. As the plates are shifted, the filter cake falls from each chamber into a cake hopper or drum below the press. A spatula can be used to scrape the cake from the cloths if needed.
One of the main advantages of the recessed chamber plate design is the ability to feed a large center hole versus a small opening in the corner of the plate. The large hole in the center of the plates allows the chambers to fill faster and more evenly, with less risk of clogging and causing plate damage due to unequal pressure. This is especially important in applications with high feed solids.
However, it's also important to note that a larger feed inlet (combined with gaining one more filtrate outlet in a center feed configuration) is important in large-scale polishing applications with high flux rates (for example, a Merrill-Crowe process). If the filter plate inlets, outlets, and internal porting are not large enough, the calculated press flow rate will not be achievable.
Another advantage is the ability to achieve higher feed pressure with the recessed chamber design. The 'frame' or sealing surface of the recessed chamber plate is all connected to the center web. This keeps the 'frame' from bowing out under high pressures.
Also, filter cake release is generally easier with a recessed plate. When the press is opened, and the plates are shifted, the cake either falls out or is quickly scraped off the cloths using a spatula. Cake release may not be as fast with a plate and frame press, as the filter cake is held by a non-tapered frame and may require more manipulation for removal.
Although recessed chamber presses have several advantages over plate and frame, one disadvantage is the limitation on cake thickness, which is dictated by the depth of the chamber. Recessed chamber plates cannot be easily swapped out for a wider or narrower frame as in a plate and frame press. This makes the plate and frame design better suited for applications where testing variations in filter cake thickness is important.
Another disadvantage can be seen in changing filter cloths. The plate and frame design allows for a simple drape-over cloth, whereas recessed chamber either requires pounding filter cloths into the plates (gasketed) or securing cloths to the plates using cloth dogs and zip ties or hook-and-loop fasteners (non-gasketed).
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