Table of Contents
The main differences between a decanter and disc-stack centrifuge are:
This article compares the different technical aspects of decanter centrifuges and disc centrifuges. We will compare all the factors important to the end-user. These will include physical, operational, performance, and maintenance factors between these centrifuge types.
A decanter centrifuge is an industrial machine designed to separate solids from liquids continuously. This process is also known as de-watering or sludge thickening.
Accelerated sedimentation is the key to the operation of all centrifuges. A decanter centrifuge exerts a force up to 4,000 times that of gravity to affect this settling. High-speed rotation is the cause of this force multiplier effect. This differential centrifugation is a widely used physical phenomenon.
As shown in the image below, the rapid rotation of the bowl causes a high centrifugal force in a radially outward direction, i.e., away from the rotating axis of the bowl. This force causes the denser solid particles to move towards the bowl wall (outward) while displacing the liquid inward.
The auger (also known as screw, scroll, or conveyor) rotates within the bowl at speed different than that of the bowl. A planetary gearbox attached to the decanter bowl rotates the auger.
The auger scrapes or pushes the collected solids towards the tapered end of the decanter. Here the solids are pushed up the ‘beach’ and exit the bowl through the solids discharge ports.
The path of the solids along the ‘beach’ is against the centrifugal force, which is directed radially outwards. This force causes the liquid to separate from the solids causing dry solids to exit the bowl.
The separated liquid(s) create a ‘pond’ inside the accumulated solids layer around the bowl periphery. Liquid discharge ports located at the far end of the bowl allow the separated liquids to exit the bowl.
A detailed writeup on decanter centrifuges is on our blog Decanter Centrifuge details, including uses, benefits, capacities, price-range, etc.
Similar to the decanter centrifuge described above, a disc centrifuge is an industrial fluid separating machine. It is designed to separate liquids from solids and liquids from liquid continuously.
A disc or disk centrifuge is also known as a conical plate, cone, disc bowl centrifuge. You can read more about disc centrifuges on Wikipedia.
Fast rotation of the disc centrifuge bowl generates very high centrifugal forces within the centrifuge bowl. These high centrifugal forces cause differential settling of the different liquid phases within the process fluid. A disc centrifuge can generate up to 10,000 times the force of gravity.
The disc centrifuge bowl cross-section shown below helps explain the operation of this type of centrifugal separator.
The bowl rotation causes a centrifugal force to act on the liquids and solids inside the bowl. This force acts in the horizontal direction away from the bowl axis of rotation.
As in the case of the decanter above, the solids are pushed towards the bowl wall. The lighter liquid phases are displaced inwards towards the center of the bowl. In case there are two immiscible liquids present, the denser liquid settles towards the solids replacing the lighter fluid towards the bowl center.
A disc centrifuge bowl has separate liquid discharge passages built into the bowl. The separated liquid phases flow through these passages to exit the centrifuge. This separation of liquids is a continuous process while the centrifuge is operating.
Self-cleaning disc centrifuges incorporate a moving part in the bowl bottom. A hydraulic mechanism causes this ‘sliding piston’ to move vertically. The downward movement of the sliding piston opens ports around the bowl periphery.
The high centrifugal force causes the accumulated solids to eject out through these ports. This solids ejection constitutes the sludge-ejection part of the self-cleaning bowl. It should be noted that the process of sludge ejection occurs while the bowl is rotating at operating speed.
A PLC-based control system triggers the sludge ejection process at predetermined time intervals.
In the following sections, we will compare the features, capabilities, and operating considerations of the decanter and disk centrifuges. We have summarized the factors in tables in each section below.
This comparison should help the user select the right centrifuge given the user’s intended use and operating conditions.
The basic physical characteristics of each centrifuge type give the user an idea of the overall sizing, weight, layout, etc. This should help envision the centrifuge in an existing plant layout or to plan a new application setup.
There is a primary difference between the orientation of the decanter and disc centrifuge. The orientation of the centrifuge influences the inlet & outlet connection locations as well as the foot-print of the system.
Decanter centrifuges are also known as horizontal centrifuges. The bowl of the decanter centrifuge rotates around a horizontal axis. The inlet-outlet on the centrifuge are therefore at either end of this rotating assembly.
The horizontal orientation is the reason for decanters to have a long foot-print and comparatively short vertical dimension or height.
Disc centrifuges are also known as vertical centrifuges. The bowl of the Disc centrifuge rotates around a vertical axis. The inlet-outlet from and to the centrifuge is located at the top of the disc centrifuges.
The inlet-outlet from and to the centrifuge is located at the top of the disc centrifuges. The vertical orientation is the reason for disc centrifuges to have a relatively smaller footprint compared to a decanter centrifuge of similar capacity.
It is important to note that the sizes and weights mentioned below are rough estimates and could vary considerably based on the manufacture, vintage, and accessories (if any) attached to the centrifuge.
Due to their horizontal orientation, decanter centrifuges tend to have one long dimension and relatively shorter height.
A small (~5 GPM) decanter centrifuge measures 5’ (L) x 2’ (W) x 3’ (H) and weighs around 800 Lbs.
A large capacity decanter (~1,000 GPM) is around 18’ (L) x 8’ (W) x 6’ (H) and could weigh over 20,000 Lbs.
Due to their vertical orientation, Disc centrifuges tend to have a smaller footprint with a taller dimensional profile.
A small (~5 GPM) disc centrifuge measures 3’ (L) x 3’ (W) x 5’ (H) and weighs around 1000 Lbs.
A large capacity disc centrifuge (~300 GPM) is around 6’’ (L) x 5’ (W) x 8’ (H) and could weigh over 4,000 Lbs.
Power ratings for centrifuges are based on the drive motor horsepower of the machine. Accessories such as inline electric heaters can add additional power load, often more than the centrifuge motor.
For this comparison, we compare the main motor power between the two types of centrifuges.
The smallest decanter centrifuge operates on a 10 HP motor. Large capacity decanters (municipal wastewater) are driven by motors rated over 500 HP. Like most industrial systems, these operate on 460 V, 3-phase power.
Disc centrifuges have smaller processing capacities as compared to the smallest decanter centrifuges. The smallest disc centrifuge (~ 2GPM) has a 1.5 HP motor drive. Disc bowl centrifuges also operate on 460 V, 3-phase power.
For customer-specific needs, small disc centrifuges can be modified to be driven by low-voltage, single-phase motors. This adaptation requires centrifuge frame modifications.
Small decanters cannot be modified to operate on single-phase power.
The material of the centrifuge bowl is of primary concern to centrifuge users. The frame components are mostly made of cast iron or a carbon steel welded frame. The bowl parts are the ones in contact with the process fluid and are therefore of interest.
Decanter centrifuges manufactured by reputed companies almost always have stainless steel bowls. These are typically made of 316L duplex stainless steel.
The scroll (auger) is also made out of 316L stainless steel. However, scroll flights are spray-coated with tungsten carbide hard-surfacing for erosion protection.
Sludge discharge nozzles and other areas subject to wear have stellite or similar erosion resisting inserts installed on them.
Self-cleaning disc centrifuges also have 316L stainless steel as the main bowl material. User needs to be aware that not all stainless steel is the same.
There are known instances of some centrifuges having bowls referred to as being stainless steel which could be technically correct. However, low-grade stainless steels are not suitable for centrifuges and corrode easily in use.
Disc centrifuges are also equipped with liners to protect the bowl parts which are likely to erode. Replaceable bowl liners help protect high wear areas of the bowls.
Marine-grade centrifuges also have some bowl parts made of ‘red metal’ which is a copper alloy with a significant amount of tin to ensure durability.
The following table summarizes all the above-mentioned characteristics.
|Summary of Physical Characteristics
|Physical Characteristics||Decanter Centrifuge||Disc Centrifuge|
|Axis of Rotation (Orientation)||Horizontal||Vertical|
|Foot-print (Size)||4′ x 2′ x 4′ (H) (Small 5 GPM Unit)
to 20′ x 5′ x 15′ (H) (1000 GPM Municipal Wastewater Model)
| 2′ x 2′ x 2′ (Small Diesel Unit) to
40′ Shipping Containers (with multi-unit skids)
|Drive Power||5 HP for small 5 GPM Unit to 500+ HP for Large Municipal Units||1 HP for a small unit to 100 HP for Large Disc Centrifuges|
|Material of Construction (MOC)||Frame Cast-Iron, Bowls Mostly Stainless Steel with Erosion Protection of Wear Parts||Frame Cast-Iron, Bowls Mostly Stainless Steel with Some non-Ferrous Parts|
Particle separation efficiency is defined as the minimum particle size; a centrifuge can separate under normal operating conditions. Of course, this efficiency changes with residence time the fluid inside the bowl.
Higher residence time (i.e., lower flow-rate) will lead to the separation of smaller particles. Lower fluid viscosity also will have a similar effect.
For this comparison, we will assume that all external factors are equal.
Particle separation efficiency for a decanter centrifuge is in the range of 50 microns and above. This particle size is an approximate range suggested by the OEM. However, based on our field experience, the actual particle size separated by decanters seems to be in the 100+ micron range.
The largest particle size separated by the decanter is defined by the size of the internal fluid pathways and sludge ejection ports. The maximum particle size for the decanters is approximately 12 mm (½”).
A disc centrifuge can separate metal particles down to a 0.5-micron level and Organic and inorganic particles down to a 1-micron level based on OEM data. These separations are dependent on the fluid being processed, specifically the viscosity of the process fluid.
The largest particle size separated by a disc centrifuge is defined by the spacing between the conical plates (disk stack) in the centrifuge bowl. The solid particles pass through these discs, and therefore the particle size cannot be larger than the inter-disc spacing.
The particle limit recommended for the disc-stack centrifuge is around 250 microns. The typical inter disc spacing is 500 microns in a disc centrifuge bowl.
Particles larger than the inter-disc spacing or close to the inter disc spacing can cause the conical discs to get plugged with solids and make the centrifuge ineffective.
Feed solids concentration refers to the amount of solids present in the incoming fluid feed. Different centrifuge types have varying ability to handle solids loading.
Solids concentrations allowable in the centrifuge feed is defined by the sludge ejection mechanism used in the centrifuge. Higher solids concentration requires a continuous sludge ejection mechanism, while intermittent ejections can handle smaller solids concentration.
The decanter centrifuges (as described above) have the auger pushing out the separated solids continuously through the sludge ports. This continuous evacuation of solids allows for the handling of high levels of solids concentration in the feed.
A decanter centrifuge can handle up to 50% solids concentration by volume. Other considerations that affect this limit include the type and density of solids. Denser, heavier solids create a higher resistance to the auger pushing the solids.
This resistance, in turn, causes higher torque on the gearbox, which has a defined torque-limit. This means that the heavier solids should be at a lower concentration than lighter solids to prevent damaging the gearbox.
For example, a decanter may handle up to 50% concentration of light solids but not more than 15% concentration of very heavy solids.
A disc centrifuge bowl has a pre-defined sludge holding space. Once this space gets filled up with separated solids, the sludge needs to be discharged. The separated solids are ejected intermittently by operating the sludge discharge mechanism.
The fixed sludge space and intermittent nature of the discharge imply that higher solids concentration leads to frequent sludge discharge cycles.
Each sludge discharge cycle is accompanied by:
Based on the above factors, it is advisable to minimize the frequency of the sludge discharge cycles, limiting the allowable solids concentration. The maximum solids concentration allowable in a disc centrifuge is around 5% by volume in real terms.
If the anticipated concentration of solids is slightly higher, a larger capacity centrifuge may be better suited. A larger capacity centrifuge bowl has a larger sludge holding capacity, which reduces the sludge discharge frequency.
Phases are the different constituents of the process fluid. For example, fluid in a diesel storage tank has 3-phases. These would be the diesel fuel (liquid phase), water (liquid phase), and sludge (solid phase).
In the case of liquid-liquid separation, a disc centrifuge is recommended. This recommendation is because a disc centrifuge generates a much higher g-force (than a decanter), which is essential for liquid-liquid separation.
If the liquids have very similar specific gravities, the disc centrifuge can magnify this specific gravity differential to affect good separation.
A decanter centrifuge has limited applicability in liquid-liquid separation due to its lower centrifugal force. Especially if there are no solids or minimal solids, a disc centrifuge would be the obvious choice.
In cases involving the separation of liquids and solids, centrifuge choice depends on the solids concentration and particle size.
A high solids concentration (over 10%) rules out the standard ‘self-cleaning’ disc centrifuge, as explained above. In such cases, a decanter centrifuge is an obvious choice. Decanter centrifuges are often the only solution for high solids concentration fluids such as oil sludge.
However, if the solids concentration is within the disc centrifuge’s allowable limits, the disc centrifuge would be recommended. This suggestion is due to the disc centrifuge’s better separation efficiency, which will produce a much clearer centrate than a decanter centrifuge.
Separation of contaminated diesel fuel is an example of a liquid-liquid-solid application. Typically in this application, the solids concentration is low, and water could be as high as 50%. Since the disc centrifuge discharges the separated water continuously, high water levels do not impede the use of a disc centrifuge.
In cases where the process fluid has a high level of solids, a 3-phase decanter (also known as a tricanter) is recommended. The tricanter is a decanter centrifuge with the addition of an additional liquid phase outlet.
As explained above, the tricanter has a lower centrifugal force leading to a lower liquid-liquid separation ability. The lower centrifugal force also allows smaller (< 100-micron level) particles to pass through the tricanter.
Therefore, it follows that in an ideal setup, a downstream disc centrifuge processes the centrate from the tricanter. The disc centrifuge separates the finer particles and clarifies the tricanter effluent under the higher g-force.
The following table summarizes all the factors mentioned earlier.
Summary of Separation Capabilities and Features
|Separation Capability||Decanter||Disc Centrifuge|
|Particle Separation Efficiency||From 50 µ to 10+ mm||From < 0.5 µ to 1 mm|
|Feed Solids Concentration||Up to 50% (v/v)||Not > 8% (v/v)|
|Liquid Liquid Separation||Somewhat Effective||Highly Effective|
|Liquid-Solid Separation||Effective for Bulk Solids||Effective for Small Particles|
|Centrifugal Force (RCF)||2,500 Gs to 4,000 Gs||7,000 Gs to 10,000+ Gs|
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Prospective users of centrifuges will want to consider the following operating factors for each type of centrifuge. These factors play an essential role in further differentiating the decanter centrifuge from the disc centrifuge.
The solids discharge mode is the method by which a centrifuge ejects or discharges the separated solids. It is an essential consideration because it affects the process layout upstream and downstream of the centrifuge. Therefore it should be considered before finalizing the centrifuge and its placement in the overall process flow.
One of the main advantages of the decanter centrifuge is the ability to eject the separated solids continuously. The scroll (auger) scrapes and pushes the solids towards and out through the solids discharge ports.
This specific feature allows the installation of the decanter centrifuge in the primary process loop in series with upstream and downstream equipment. Of course, it is always advisable to have a redundant (backup) unit in a parallel circuit to avoid process disruptions in case of machine breakdown or during maintenance.
A self-cleaning disc centrifuge has an intermittent solids discharge characteristic. This type of disc centrifuge accumulates the solids and periodically discharges them based on a programmable timer. The operator sets the sludge discharge time interval based on the incoming fluid solids concentration and bowl sludge capacity.
It is important to note that many self-cleaning disc centrifuges cannot process fluid during this sludge discharge cycle. Process flow needs to be interrupted during this period.
Therefore a disc centrifuge of this type (self-cleaning) cannot be installed in the primary process flow loop. It should be installed in a ‘kidney loop’ configuration or with pre and post centrifuge surge tanks to accommodate for the loss of flow during the discharge cycle.
The basic design of the centrifuges involves several rotating parts (also known as rotating assembly or RA). There some intricacies involved in the construction of these centrifuges, which are essential to the functioning of the centrifuges. These design characteristics also add to the respective mechanical complexity of the machines.
A decanter centrifuge has a more straightforward construction compared to the disc centrifuge. It is essentially a rotating drum with an internal rotating auger with relatively fewer parts and no moving interfaces between these parts.
The most complicated part of a decanter centrifuge is the planetary gearbox. Most of these gearboxes are 2-stage with sets of planetary gears on rotating hubs.
The more straightforward design of decanter centrifuges leads to more accessible and quicker service. It also means fewer replacement parts compared to disc centrifuges.
The ‘self-cleaning’ disc centrifuges have an added internal system that facilitates the sludge discharge process. This system is a hydraulic mechanism that uses water to operate the movement of the sliding piston shown in the section above.
This additional mechanism, which is not present in decanter centrifuges, adds a certain degree of complexity to the disc centrifuge. It also means that the bowl has extra serviceable parts.
Centrifuge control systems are essential for the reliable and efficient operation of centrifuges. Centrifuge design characteristics define these control systems. Some control features are application-specific and are applicable across different centrifuge types.
Basic controls for decanter centrifuges involve motor control and monitoring of field sensors. These are relatively simple controls without the need for a logic controller (PLCs). The essential operation of the decanter centrifuge is s simple sequence of motors.
Some additional control logic may be added based on instrument and sensor feedback to prevent malfunction or system overload.
A disc centrifuge control system is slightly more sophisticated as compared to the decanter control system. As previously mentioned, the disc centrifuge has an additional sub-system for sludge ejection. This system requires an extra water manifold to operate the hydraulically operated piston.
There is a sequence of operations associated with the sludge ejection system. A programmable controller (PLC) is the best option to operate this system.
Other functional and alarm systems, similar to the ones for the decanter centrifuge, are also incorporated into the disc centrifuge control system.
The addition of auxiliary systems enhances centrifuge performance. Such add-on systems include fluid heaters, filters, heat exchangers, etc. However, the operation of centrifuges requires some auxiliary systems. In this section, we discuss these ‘required’ systems briefly.
Some decanter centrifuges need auxiliary systems for regular operation. These systems are essential for operating the centrifuge. These systems include hydraulic packs for decanter centrifuge back-drive control. Additionally, they need a lubrication system for decanter centrifuge bearings and an electric motor for auger speed control.
However, depending on the design, some decanter centrifuges can be operated without any auxiliary systems. In such cases, the bearings are grease lubricated, and the back-drive is ‘locked’ to give a fixed differential speed.
A disc centrifuge (self-cleaning type) requires a hydraulic system for the operation of the sludge ejection mechanism. A disc centrifuge cannot function without the operating water system controlled by this auxiliary system.
Other auxiliary systems such as alarms systems, temperature and pressure indicators, etc. are useful but not essential for the operation of the disc centrifuge.
The following table summarizes all the factors mentioned above.
|Summary of Operating Considerations|
|Property||Decanter Centrifuge||Disc Centrifuge|
|Solids Discharge / Ejection||Continuous Mode||Batch Mode (Self-Cleaning type)|
|Design Complexity||Less Complex, Simpler Construction||More Complex, More Moving Parts|
|Control System||VFD Control for Main Drive Motors. Safety Devices Monitoring System.||PLC Based Control System with Operating Sequence Logic.|
|Auxillary Systems Required||Lubrication Pack and Hydraulic Unit for Backdrive Control (large units)||Operating Water System (Self-Cleaning type)|
Operation and maintenance (O&M) of centrifuges is an essential factor in the return on investment (ROI) considerations of these capital-intensive machines. Lifespan i.e., durability, ease, frequency, and cost of maintenance, are key factors to be considered.
Centrifuge equipment durability is an essential factor to consider when choosing centrifuges. A comparison of centrifuges with other forms of separation equipment is common. These include filters, filter presses, screw presses, belt presses, etc.
Durability is the useful lifespan of capital equipment combined with the need and frequency of maintenance.
Decanter centrifuges are possibly some of the most durable processing equipment available. Some of the well-known manufacturers (Alfa Laval, Sharples, and Westfalia) are globally popular primarily due to the durability of their machines.
It is not uncommon to find a functioning decanter centrifuge, which is over 40 years old!
Decanter centrifuges from these manufacturers are well known for their heavy-duty design and unusually long service lives.
Although disc centrifuges are more sophisticated in their construction as compared to decanter centrifuges, they are equally durable and long-lasting. Again, disc centrifuges manufactured by the established brands are known for their durability.
The durability of these machines is attributed to their design and material of construction. Amongst disc centrifuges, the older generation machines are even more durable than some of, the newer versions. This durability is mainly due to the heavy-duty gear transmissions in the older disc centrifuges.
Users prefer gear-driven disc centrifuges despite their age. Their simple construction leads to longer, dependable service life. In other words, they have a lesser number of parts compared to the newer disc centrifuges, which means less frequent breakdowns and longer up-time.
As with all mechanical systems, periodic maintenance is another crucial factor to consider during the selection process. We have summarized the scope and related expenses for the centrifuges of interest.
Maintenance frequency is dependent on the use of the equipment. We intend to provide a summary of recommended maintenance under normal operating conditions.
The gearbox is one of the critical components of the decanter centrifuge. Therefore preventative maintenance of the gearbox has an impact on the trouble-free operation of the machine. Changing the oil is the best way to ensure the longevity of the gearbox and the equipment.
Lubrication (greasing) of the bearing housings on the decanter is the other crucial preventative maintenance that should be performed regularly.
Replacement of the seals, gaskets, and bearings is typically required once every few years (2 ~ 3 years) depending on the severity of the service duty.
The cost of maintenance for decanters is relatively meager given there are no consumable parts or media to be replaced frequently.
One of the keys to the maintenance of a disc centrifuge, similar to the decanter centrifuge, is to keep the transmission gearbox lubricant clean. A disc centrifuge has a soft-metal bull gear that wears and releases fine metal particles in the oil.
Changing the oil frequently ensures the longevity of the bearings. The recommended frequency of oil-change for many disc centrifuges is 1000 operating hours after the first oil changes.
It worth noting that it is easy to replace the oil than to change bearings more frequently than necessary.
For disc centrifuges, it recommended performing a bowl service (replace all seals) on a set schedule, which depends on the type of centrifuge and the service application. This period could be as frequent as every other week for abrasive fluids to once every few months for benign applications.
The cost of maintenance parts for disc centrifuge is low, considering the fluid volume processed in the period between servicing. Also, there are no filter media to be replaced, which helps lower maintenance costs.
The table below is a summary of all these factors to be considered.
|Operation & Maintenance Factors|
|Factor||Decanter Centrifuge||Disc Centrifuge|
|Durability||Highly Durable with Regular PM
50+ Years Service Life Common
|Very Durable with Regular PM
50+ Years Service Life Common
|Maintenance Cost||Very Low, Bearings Replacement Over Long Periods.||Low, Inexpensive Seal Kit Periodically Replaced.|
|Maintenance Scope||Grease Bearings, Replace Gearbox Oil.||Replace Bowl Seals & Oil in Gear Housing.|
Based on all the above-listed considerations, we can summarize the differences as follows.
Decanter centrifuges can handle fluids with high sludge content with large particle sizes. They are the ‘first line of defense’ in any industrial fluid separation application with heavy sludge.
Disc Centrifuges can separate fluids with two immiscible liquids continuously. With a higher centrifugal force, disc centrifuge is ideal for removing fine particles as well.
We should also mention that a decanter centrifuge can separate fine solids given enough retention time. In other words, a low flow rate. But the flow-rate to achieve that level of separation defeats the purpose of the decanter centrifuge.
Contact Dolphin Centrifuge to consult with our centrifuge experts to discuss your application. You can always call (248) 522-2573 to reach us.