mud pump suction line strainer brands

The HURRICANE suction line strainer protects mud pump fluid ends from unwanted debris entering the fluid stream. The strainer is easily cleaned and returned to service in minutes. A variety of end connections are available, including butt weld, flanged or threaded, to install in the suction line of any mud pump. HURRICANE strainers are built to withstand the rough service found on drilling rigs. Inlet / outlet diameters of 4”, 6”, 8”, 10” and 12” are standard. Provide the inlet / outlet size and height D as shown below with any price requests.

We offer pump strainers that are great at preventing large particles of sediment, sewage, mud, or solids from entering the suction port of drainage pumps. These strainers are great for use in swimming pools, pit blinds, or any other situation where you are pumping out water that is not clean. we offer 2 inch, 3 inch, and 4 inch strainers to fit all of the different size pumps. These strainers go great with our Koshin pumps. If you have any questions regarding strainers feel free to call us at 800-488-9146 or email us at orders@frankwall.com.

A wide variety of pump strainer mud pump options are available to you, such as 1 year, not available and 3 years.You can also choose from new, pump strainer mud pump,As well as from energy & mining, construction works , and manufacturing plant. And whether pump strainer mud pump is 1.5 years, unavailable, or {3}.

One of the most important pieces of equipment in many different industries is the filtration system. Within each filtration system are a number of moving parts, which must all work together to ensure the system operates efficiently. Two parts that rely on each other the most are pumps and strainers. As the pump works, the strainer is in place to capture debris to ensure the pump can continue to function as designed.

Typically, when one refers to a hydraulic pump strainer, they are referring to a mesh strainer that is used as a filter at the pump inlet. The purpose of this strainer is to filter contaminants out of the hydraulic fluid as it approaches the suction side of the pump. These relatively coarse filters (about 140 microns) screw onto the pump intake, which is located inside the hydraulic reservoir.

Like we said above, the main purpose of a strainer is to filter out any solid contaminants from hydraulic fluid. If contaminants are left unfiltered, they can damage components of the pump. When the pump is damaged it can lead to lower system efficiency and a shortened lifespan.

That being said, picking the incorrect strainer for your system can also damage the pump. When selecting a strainer, it’s important to first consult the manufacturer recommendations. You also need to ensure you’ve selected the right sized filter, and one that meets your systems pressure and flow requirements. If your strainer fails to meet those requirements, you could potentially cause irreversible damage to your system.

The positioning of your strainer first and foremost depends on the type of strainer your system requires. The two most common types are pump suction strainers and inline filters. Pump suction strainers are a coarse mesh strainer that is used to collect large participles from entering the pump. They are installed at the suction inlet of the pump. Inline filters, sometimes called return line filters or spin-on filters, are installed in the fluid return line. This filter allows for a finer filtration of particles than the pump suction strainer and results in a highly efficient filtration system. Inline filters are not installed on the suction side of the pump because this can cause pump failure from high differential pressure.

Most pumps are designed to handle some number of solids, and the manufacturer can advise you on what size particles your pump can handle and may even have a suggestion on what filtration type is best for the system. Ultimately, the positioning of your strainer will depend on what type of system you have and how fine of a filtration you require.

While the strainer is an important part of a filtration system, there are instances where strainers are unnecessary. If the hydraulic fluid being placed into the system has already been filtered, it is unnecessary for it to be filtered again within the system. Additionally, some new hydraulic systems do not even require a strainer as the updated design minimizes the chance of debris. Though, if proper maintenance isn’t done on the system you could still experience pump damage.

There’s no other way to argue it: strainers are important to a pump system. It’s the choice of a strainer and the positioning of that strainer that can be up for debate sometimes. If you’re questioning where to place a strainer in your system, or what strainer to use, first consult the manufacturer for their recommendations. If you still have questions after that, consult a qualified suction strainer/filter designer.

Strainers are designed to remove large contaminants (defined as 40-microns or greater) from the material being processed. The ratio of mesh to microns changes depending on the number of gaps within one linear inch. For example, 60-mesh strainers typically catch particles around 240-microns, and 100-mesh strainers catch particles sized at 150-microns.

There are a number of different advantages to using this type of strainer. The easy-to-open design of the strainer provides for simple maintenance. Simplex strainers also have a large particle holding capacity with less pressure drop over the length of the filter element.

At Eaton, Simplex Industrial Basket Strainers are designed to be used where it is possible for the line to be shut down for short periods of time to allow for maintenance. Eaton’s standard cast pipeline strainers meet a number of high standards. These include ISO 9001-2008 quality management, reduced purge volumes due to their ultra-low discharge strainer technology, and appropriately sized parts to meet any flow rate and retention requirement. To learn more, check out our website.

The advantages of this type of strainer lie in the price, as Y strainers are commonly low cost. Maintenance for this type of strainer can be a little tricky, and particle retention capacity is low.

One of the biggest advantages of duplex strainers is their ease of maintenance. Not only do duplex strainers have an easy-open design, they are also able to be cleaned individually while one strainer stays on standby. In addition to an easier maintenance, duplex strainers have high particle holding capacity, which provides less pressure drop through the strainer. To get more specifications, peruse our selection of duplex strainers here.

Eaton’s Duplex Industrial Basket Strainer is able to operate on a continuous basis, never requiring the line to stop for maintenance tasks to be performed. This is due to the two baskets being used, which operate independently of one another. Once one of the baskets becomes full, the flow is channeled to the other basket, allowing the full basket to be removed and cleaned out. The design of Duplex Industrial Basket Strainer makes it a great option for applications where lines cannot be shut down for maintenance to take place. Visit our site to learn more.

The main advantage of using an automatic strainer is their self-cleaning capabilities. Because of the automatic nature of the strainer, the cleaning process is never interrupted. Instead, self-cleaning is controlled in a number of different ways, most commonly timers, pressure drop settings, or manually. Contact us today to find out your options.

Gas and oil strainers can be utilized in a number of different areas. Most commonly, strainers are used either in upstream or downstream applications.

Upstream applications include those for drilling oil. Strainers are used in the derrick/mast, drawworks and top drive. They are also used in mud/fuel tanks and within power/pump stations and within the shaker unit.

Strainers are designed to capture solid particles and other solid contaminants within a liquid and stop them from continuing through the system. When functioning properly, strainers help prevent potential damage to other parts of the system, including engines, pumps, nozzles, and heat exchangers. With better performing strainers, cost of ownership decreases while lifecycle of the equipment being used is extended, benefitting producers in the long run.

Pump inlet strainers are common parts for all airless sprayers. Many inlet strainers are compatible with sprayers that are not listed above. Consult your parts manual to ensure the correct strainer is purchased

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Premium Oilfield Technologies takes the responsibility of listening to our clients’ concerns very seriously. Acting on those needs enables Premium to offer robust solutions to customer issues at the rig. The Caliber® DS-7500 Fluid Ends bring together our years of field experience and unmatched client interface to represent the NEW standard for your Gardner Denver pumps.

Across any pumping system there is a complex pressure profile. This arises from many properties of the system: the throughput rate, head pressure, friction losses both inside the pump and across the system as a whole. In a centrifugal pump, for example, there is a large drop in pressure at the impeller and an increase again within its vanes (see diagram). In a positive displacement pump, the fluid’s pressure drops when it is drawn, essentially from rest, into the cylinder. The fluid’s pressure increases again when it is expelled.

If the pressure of the fluid at any point in the pump is lower than its vapour pressure, it will literally boil, forming vapour bubbles within the pump. The formation of bubbles leads to a loss in throughput and increased vibration and noise but the big danger is when the bubbles pass on into a section of the pump at higher pressure. The vapour condenses and the bubbles implode, releasing, locally, huge amounts of energy. This can be very damaging, causing severe erosion of the pump’s components.

To avoid cavitation, you need to match your pump to the fluid, system and application. This is a complex area and you are advised to discuss your application with the pump supplier.

To avoid cavitation, the pressure of the fluid must be maintained above its vapour pressure at all points as it passes through the pump. Manufacturers specify a property referred to as the Net Positive Suction Head Required or NPSH-R – this is their minimum recommended fluid inlet pressure, expressed in metres. The documentation supplied with your pump may contain charts showing how NPSH-R varies with flow.

In fact, NPSH-R is defined as the suction-side pressure at which cavitation reduces the discharge pressure by 3%. So, in designing the suction-side pipework for your system, you must ensure that it exceeds the manufacturer’s NPSH-R rating for the operating conditions. Your calculated value is termed the NPSH-Available (NPSH-A).

Remember, a manufacturer’s NPSH-R rating is the minimum recommended inlet head pressure: a pump is already experiencing cavitation at this pressure. Consequently, it is important to build in a safety margin of 0.5 to 1m to take account of this and other factors such as:

Pumps, and especially centrifugal pumps, work most efficiently when the fluid is delivered in a surge-free, smooth, laminar flow. Any form of turbulence reduces efficiency and increases wear and tear on the pump’s bearings, seals and other components.

There should be at least 5 pipe diameters’ worth of straight piping connecting to the pump. Never connect an elbow, reducer, valve, or strainer within this final run of pipework. If you connect an elbow directly to the pump flange, the fluid is effectively centrifuged towards the outer curve of the elbow and not directed into the centre (the eye) of the impeller. This creates stress on the pump’s bearings and seals which often leads to wear and premature failure.

Sometimes, it’s just not possible to make provision for a sufficient settling distance in the pipework before the pump. In these cases, use an inline flow conditioner or straightener.

It’s standard practice to employ suction-side piping one or two sizes bigger than the pump inlet - you should certainly never use any piping that is smaller than the pump’s inlet nozzle.

Small pipes result in larger friction losses, which means it costs more to run your pumping system. On the other hand, larger diameter pipes are more expensive – so you need to weigh up the increased cost with the likely energy saving resulting from reduced friction losses.

Larger pipework means that you’ll need a reducer before the pump inlet. A reducer is a constriction and requires careful design to avoid both turbulence and the creation of pockets where air or vapour might collect. The best solution is to use an eccentric reducer orientated to eliminate the possibility of air pockets.

As a general rule of thumb, suction pipe velocities should be kept below 2 m/s. At higher velocities, the greater friction causes noise, higher energy costs and increasing erosion, particularly if the fluid contains suspended solids. If your system contains any narrow pipes or other constrictions, bear in mind that the pipe velocity will be a lot higher at these points.

It’s best to keep air or vapour out of the pipework. Entrained gases cause a loss in pump performance, increase noise, vibration and component wear and tear. It’s therefore important to position the feed pipe correctly in the tank or vessel. It should be fully submerged. If it’s too close to the surface of the fluid, the suction creates a vortex, drawing air (or other vapours) into the liquid and through the pumping system. The feed pipe should also be clear of any other pipes, agitators or stirrer-paddles – anything that might drive air into the fluid. In shallow tanks or ponds, it may be advisable to use a baffle arrangement to protect the feed pipe from air entrainment.

You should also make sure that the feed pipe isn’t too close to the bottom of the tank or pond. If it is, the suction may draw up solids or sludge instead of air or vapour! The fluid may contain suspended solids in any case.

Some displacement pumps can cope with a mixed phase supply without any damage or major loss in performance. Centrifugal pumps are not so robust and must be protected from solids. In this situation you’ll need to install a filter or strainer. Filters can create a large pressure drop and be responsible for cavitation and friction-loss. The filter screen should have at least three times the free area of the pipe cross-section. Use a differential pressure gauge across the screen to look out for any increased pressure drop before clogging problems arise. This will also help in the accurate assessment of NPSH-A.

Obviously, pumps should be securely located - but so should the pipework. Don’t use one to support the other. All other components must be just as securely located and create no stresses or strains on any other parts of the system. Ensure that the pipe connecting to the pump’s inlet flange is aligned precisely with it. If you need to install non-return valves or flow control valves fit them on the discharge side of the pump, and never in suction-side pipework.

Ensure that conditions do not favour cavitation, particularly if you are using a centrifugal pump. This requires careful selection of the pump, its positioning and the head pressure.

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One of Forum’s most committed core values is that “no one gets hurt,” and the P-Quip system is designed to support that principle. Streamlined and easy to use, it reduces or eliminates the need for manual force during maintenance, shrinking the time needed to replace high-use components and minimizing safety risks.