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Fouling

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2330:. They are distinguished from fouling deposits, which form from material originating ex-situ. Corrosion deposits should not be confused with fouling deposits formed by ex-situ generated corrosion products. Corrosion deposits will normally have composition related to the composition of the substrate. Also, the geometry of the metal-oxide and oxide-fluid interfaces may allow practical distinction between the corrosion and fouling deposits. An example of corrosion fouling can be formation of an iron oxide or oxyhydroxide deposit from corrosion of the carbon steel underneath. Corrosion fouling should not be confused with fouling corrosion, i.e., any of the types of corrosion that may be induced by fouling. 2610:. The periodic sharp variations in the apparent fouling amount often correspond to the moments of system shutdowns, startups or other transients in operation. The periodic variations are often interpreted as periodic removal of some of the deposit (perhaps deposit re-suspension due to pressure pulses, spalling due thermal stresses, or exfoliation due to redox transients). Steam blanketing has been postulated to occur between the partially spalled deposits and the heat transfer surface. However, other reasons are possible, e.g., trapping of air inside the surface deposits during shutdowns, or inaccuracy of temperature measurements during transients ("temperature streaming"). 691: 2564:- This can occur when fouling rate is quantified by monitoring heat transfer. Relatively small amounts of deposit can improve heat transfer, relative to clean surface, and give an appearance of "negative" fouling rate and negative total fouling amount. Negative fouling is often observed under nucleate-boiling heat-transfer conditions (deposit improves bubble nucleation) or forced-convection (if the deposit increases the surface roughness and the surface is no longer "hydraulically smooth"). After the initial period of "surface roughness control", the fouling rate usually becomes strongly positive. 2385: 2481:
The normalized fouling rate (also in kg/ms) will additionally account for the concentration of the foulant in the process fluid (kg/kg) during preceding operations, and is useful for comparison of fouling rates between different systems. It is obtained by dividing the fouling rate by the foulant concentration. The fouling rate constant (m/s) can be obtained by dividing the normalized fouling rate by the mass density of the process fluid (kg/m).
667: 58: 375: 2620: 683: 3582:, cleaning with high-velocity water jets ("water lancing"), recirculating ("blasting") with metal, sponge or other balls, or propelling offline mechanical "bullet-type" tube cleaners. Whereas chemical cleaning causes environmental problems through the handling, application, storage and disposal of chemicals, the mechanical cleaning by means of circulating cleaning balls or offline "bullet-type" cleaning can be an 3296: 363: 170: 155: 3403:. Some plants employ foreign-object exclusion program (to eliminate the possibility of salient introduction of unwanted materials, e.g., forgetting tools during maintenance). Acoustic monitoring is sometimes employed to monitor for fretting by detached parts. In the case of micro fouling, water purification is achieved with extensive methods of water treatment, 3196:. The underlying physical picture for this model is that of a two-layer deposit consisting of consolidated inner layer and loose unconsolidated outer layer. Such a bi-layer deposit is often observed in practice. The above model simplifies readily to the older model of simultaneous deposition and re-entrainment (which neglects consolidation) when λ 2600:- In this scenario, the fouling rate increases with time; the rate of deposit buildup accelerates with time (perhaps until it becomes transport limited). Mechanistically, this scenario can develop when fouling increases the surface roughness, or when the deposit surface exhibits higher chemical propensity to fouling than the pure underlying metal. 3570:) are an option for some applications. Modern components are typically required to be designed for ease of inspection of internals and periodic cleaning. On-line fouling monitoring systems are designed for some application so that blowing or cleaning can be applied before unpredictable shutdown is necessary or damage occurs. 537:, the ingress of macro fouling into the cooling tower basin is possible through open canals or by the wind. Sometimes, parts of the cooling tower internals detach themselves and are carried into the cooling water circuit. Such substances can foul the surfaces of heat exchangers and may cause deterioration of the relevant 915:
temperature and thus will foul the cooling surfaces. Salts with "inverse" or "retrograde" solubility will foul the heating surfaces. An example of the temperature dependence of solubility is shown in the figure. Calcium sulfate is a common precipitation foulant of heating surfaces due to its retrograde solubility.
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Bacterial fouling can occur under either aerobic (with oxygen dissolved in water) or anaerobic (no oxygen) conditions. In practice, aerobic bacteria prefer open systems, when both oxygen and nutrients are constantly delivered, often in warm and sunlit environments. Anaerobic fouling more often occurs
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This article is primarily devoted to the fouling of industrial heat exchangers, although the same theory is generally applicable to other varieties of fouling. In cooling technology and other technical fields, a distinction is made between macro fouling and micro fouling. Of the two, micro fouling is
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Precipitation fouling can also occur in the absence of heating or vaporization. For example, calcium sulfate decreases its solubility with decreasing pressure. This can lead to precipitation fouling of reservoirs and wells in oil fields, decreasing their productivity with time. Fouling of membranes
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increases because the heat exchangers have to be designed in larger sizes to compensate for the heat-transfer loss due to fouling. To the output losses listed above, one needs to add the cost of down-time required to inspect, clean, and repair the components (millions of dollars per day of shutdown
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consists of transport to the surface and subsequent attachment. Deposit removal is either through deposit dissolution, particle re-entrainment, or deposit spalling, erosive wear, or exfoliation. Fouling results from foulant generation, foulant deposition, deposit removal, and deposit consolidation.
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The most straightforward way to quantify fairly uniform fouling is by stating the average deposit surface loading, i.e., kg of deposit per m of surface area. The fouling rate will then be expressed in kg/ms, and it is obtained by dividing the deposit surface loading by the effective operating time.
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Solidification fouling occurs when a component of the flowing fluid "freezes" onto a surface forming a solid fouling deposit. Examples may include solidification of wax (with a high melting point) from a hydrocarbon solution, or of molten ash (carried in a furnace exhaust gas) onto a heat exchanger
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Other terms used in the literature to describe fouling include deposit formation, encrustation, crudding, deposition, scaling, scale formation, slagging, and sludge formation. The last six terms have a more narrow meaning than fouling within the scope of the fouling science and technology, and they
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On the component design level, fouling can often (but not always) be minimized by maintaining a relatively high (for example, 2 m/s) and uniform fluid velocity throughout the component. Stagnant regions need to be eliminated. Components are normally overdesigned to accommodate the fouling
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Composite fouling is common. This type of fouling involves more than one foulant or more than one fouling mechanism working simultaneously. The multiple foulants or mechanisms may interact with each other resulting in a synergistic fouling which is not a simple arithmetic sum of the individual
323:, organic) or a non-living substance (inorganic). Fouling is usually distinguished from other surface-growth phenomena in that it occurs on a surface of a component, system, or plant performing a defined and useful function and that the fouling process impedes or interferes with this function. 4232: 914:
on temperature or presence of evaporation will often be the driving force for precipitation fouling. The important distinction is between salts with "normal" or "retrograde" dependence of solubility on temperature. Salts with the "normal" solubility increase their solubility with increasing
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has been a subject of controversy as to its effectiveness for fouling control since the 1950s. The prevailing opinion is that it simply "does not work". Nevertheless, some studies suggest that it may be effective under some conditions to reduce buildup of calcium carbonate deposits.
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anticipated between cleanings. However, a significant overdesign can be a design error because it may lead to increased fouling due to reduced velocities. Periodic on-line pressure pulses or backflow can be effective if the capability is carefully incorporated at the design time.
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Chemical or mechanical cleaning processes for the removal of deposits and scales are recommended when fouling reaches the point of impacting the system performance or an onset of significant fouling-induced degradation (e.g., by corrosion). These processes comprise pickling with
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of the deposits will likely influence the probability of underdeposit corrosion. Deposit composition can also be important - even minor components of the deposits can sometimes cause severe corrosion of the underlying metal (e.g., vanadium in deposits of fired boilers causing
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J. Moghadasi, H. Müller-Steinhagen, M. Jamialahmadi, and A. Sharif, "Scale Deposition in Porous Media and their Removal by EDTA Injection ", ECI Engineering Conferences International Symposium Series, Heat Exchanger Fouling and Cleaning VII, July 1–6, 2007 - Tomar, Portugal.
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Piping, flow channels – reduces flow, increases pressure drop, increases upstream pressure, increases energy expenditure, may cause flow oscillations, slugging in two-phase flow, cavitation; may increase flow velocity elsewhere, may induce vibrations, may cause flow
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C.W. Turner, S.J. Klimas, "Modelling the Effect of Surface Chemistry on Particle Fouling Under Flow-Boiling Conditions", Proceeding of Heat Exchanger Fouling: Fundamental Approaches and Technical Solutions, 2001, July 8–13, Davos, Switzerland, AECL Report
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There is no general rule on how much deposit can be tolerated, it depends on the system. In many cases, a deposit even a few micrometers thick can be troublesome. A deposit in a millimeter-range thickness will be of concern in almost any application.
4201: 2511:), localized fouling, packing of confined regions with deposits, creation of occlusions, "crevices", "deposit tubercles", or sludge piles. Such deposit structures can create environment for underdeposit corrosion of the substrate material, e.g., 3362:
plants, fouling may reduce the gained output ratio by two-digit percentages (the gained output ratio is an equivalent that puts the mass of generated distillate in relation to the steam used in the process). The extra electrical consumption in
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particles, i.e., particles smaller than about 1 μm in at least one dimension (but which are much larger than atomic dimensions). Particles are transported to the surface by a number of mechanisms and there they can attach themselves, e.g., by
898: 2741: 3539:, polymethacrylic acid, usually with a molecular weight lower than 10000). For fired boilers, aluminum or magnesium additives can lower the melting point of ash and promote creation of deposits which are easier to remove. See also 2576:- In this scenario, the fouling rate decreases with time, but never drops to zero. The deposit thickness does not achieve a constant value. The progress of fouling can be often described by two numbers: the initial fouling rate (a 4047:
H. M. Herro (Nalco Chemical Company), "Deposit-Related Corrosion in Industrial Cooling Water Systems", Presented at the National Association of Corrosion Engineers Corrosion ’89 meeting, New Orleans, Louisiana, April 17–21, 1989
1711:. Note that the attachment of colloidal particles typically involves electrical forces and thus the particle behaviour defies the experience from the macroscopic world. The probability of attachment is sometimes referred to as " 4181:
Xu Zhi-Ming, ZHANG Zhong-Bin, and YANG Shan-Rang, "Costs due to utility fouling in China", ECI Engineering Conferences International Symposium Series, Heat Exchanger Fouling and Cleaning VII, July 1–6, 2007 - Tomar, Portugal.
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Fouling is ubiquitous and generates tremendous operational losses, not unlike corrosion. For example, one estimate puts the losses due to fouling of heat exchangers in industrialized nations to be about 0.25% of their
2594:). This is often the case for relatively soft or poorly adherent deposits in areas of fast flow. The asymptote is usually interpreted as the deposit loading at which the deposition rate equals the deposit removal rate. 3032: 2606:- Here, fouling loading generally increases with time (often assuming a generally linear or falling rate), but, when looked at in more detail, the fouling progress is periodically interrupted and takes the form of 2548:
Deposit on a surface does not always develop steadily with time. The following fouling scenarios can be distinguished, depending on the nature of the system and the local thermohydraulic conditions at the surface:
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In heat transfer equipment, where the primary concern is often the effect of fouling on heat transfer, fouling can be quantified by the increase of the resistance to the flow of heat (mK/W) due to fouling (termed
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D.H. Lister, ""Corrosion products in power generating systems". In: Fouling of Heat Exchanger Equipment", E.F. Somerscales and J.G. Knudsen (eds.), Hemisphere Pub. Corp., Washington, DC, USA, 1981, pp.135-200.
2558:- Sometimes, a near-nil fouling rate is observed when the surface is new or very clean. This is often observed in biofouling and precipitation fouling. After the "induction period", the fouling rate increases. 673:
buildup inside a pipe reduces liquid flow through the pipe and reduces thermal conduction from the liquid to the outer pipe shell. Both effects will reduce the pipe's overall thermal efficiency when used as a
2732:      [ rate of accumulation of unconsolidated deposit ] = [ rate of deposition ] - [ rate of re-entrainment of unconsolidated deposit ] - [ rate of consolidation of unconsolidated deposit ] 3766:
G.A. Mansoori "Physicochemical Basis of Arterial Blockage / Fouling. Prediction and Prevention." Department of Chemical Engineering, University of Illinois at Chicago, on-line publication, September 2001
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Joshua M. Hawkes, "The Simulation and Study of Conditions Leading to Axial Offset Anomaly in Pressurized Water Reactors", Georgia Institute of Technology Master of Science Thesis, December 2004.
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J.C. Cowan and D.J. Weintritt, "Water-Formed Scale Deposits. A Comprehensive Study of the Prevention, Control, Removal and Use of Mineral Scale", Gulf Publishing Company, Houston, Texas, 1976.
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Temperature dependence of the solubility of calcium sulfate (3 phases) in pure water. The water is pressurized so that it can be maintained in the liquid state at the elevated temperatures.
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Goode, Kylee R.; Asteriadou, Konstantia; Robbins, Phillip T.; Fryer, Peter J. (March 2013). "Fouling and Cleaning Studies in the Food and Beverage Industry Classified by Cleaning Type".
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Sometimes fouling autoretardation, i.e., reduction (or potentially enhancement) of crystallisation/attachment rate due to changes in the surface conditions caused by the fouling deposit;
718:. These are most often water solutions, but non-aqueous precipitation fouling is also known. Precipitation fouling is a very common problem in boilers and heat exchangers operating with 4081:
V.P. Brusakov, "Law for the Deposition of Materials on Heat-Transmitting Surfaces under the Action of Thermoelectric Effects", Atomnaya Energiya, Vol.30, No.1, pp.10-14, January 1971.
3732: 3308:. Another analysis estimated (for 2006) the economical loss due to boiler and turbine fouling in China utilities at 4.68 billion dollars, which is about 0.169% the country GDP. 2726:
For the modern model of fouling involving deposition with simultaneous deposit re-entrainment and consolidation, the fouling process can be represented by the following scheme:
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can reduce fouling in many systems, mainly by interfering with the crystallization, attachment, or consolidation steps of the fouling process. Examples for water systems are:
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Sadeghinezhad, E.; Kazi, S. N.; Dahari, M.; Safaei, Mohammad Reza; Sadri, Rad; Badarudin, A. (14 April 2014). "A Comprehensive Review of Milk Fouling on Heated Surfaces".
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Following the above scheme, the basic fouling equations can be written as follows (for steady-state conditions with flow, when concentration remains constant with time):
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Chemical reactions may occur on contact of the chemical species in the process fluid with heat transfer surfaces. In such cases, the metallic surface sometimes acts as a
1578: 3818:"Modeling PWR Fuel Corrosion Product Deposition and Growth Processes (5)", Technical Report 1009734, Electric Power Research Institute, Palo Alto, California, USA, 2004. 2370:
surface. The surface needs to have a temperature below a certain threshold; therefore, it is said to be subcooled in respect to the solidification point of the foulant.
397:, decreases heat flux, increases temperature on the hot side, decreases temperature on the cold side, induces under-deposit corrosion, increases use of cooling water; 3319:), increased pressure drop, flow blockages, flow redistribution inside components, flow instabilities, induced vibrations (possibly leading to other problems, e.g., 3694:"Marine fouling and its prevention"; prepared for Bureau of Ships, Navy Dept, Woods Hole Oceanographic Institution, United States, Navy Dept. Bureau of Ship, 1952. 2413:
Bacteria can form biofilms or slimes. Thus the organisms can aggregate on surfaces using colloidal hydrogels of water and extracellular polymeric substances (EPS) (
2238: 2211: 1836: 1809: 1536: 1507: 1478: 762: 2963:{\displaystyle {\begin{cases}{dm/dt}=k_{d}C_{m}\rho -\lambda _{r}m_{r}(t)\\{dm_{r}/dt}=k_{d}C_{m}\rho -\lambda _{r}m_{r}(t)-\lambda _{c}\cdot m_{r}(t)\end{cases}}} 3751: 4228:"Dispersants for Tube Fouling Control: Volume 2: Short-Term Trial at ANO-2", Report 1003144, Electric Power Research Institute, Palo Alto, California, USA, 2001 3558:
capability is always incorporated into steam generators or evaporators to control the accumulation of non-volatile impurities that cause or aggravate fouling.
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Deposit thickness (μm) and porosity (%) are also often used for description of fouling amount. The relative reduction of diameter of piping or increase of the
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Injection/spray nozzles (e.g., a nozzle spraying a fuel into a furnace) – incorrect amount injected, malformed jet, component inefficiency, component failure;
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The most fundamental and usually preferred method of controlling fouling is to prevent the ingress of the fouling species into the cooling water circuit. In
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occurs in cooling water for the chemical industry which has a minor content of hydrocarbons. Systems in petroleum processing are prone to polymerization of
2590:- Here, the fouling rate decreases with time, until it finally reaches zero. At this point, the deposit thickness remains constant with time (a horizontal 2361:
Fouling through an ionic reaction with an evolution of an inorganic solid is commonly classified as precipitation fouling (not chemical reaction fouling).
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A. Szkatula, M. Balanda, M. Kopec, "Magnetic treatment of industrial water. Silica activation". Eur. Phys. J.Applied Physics, 1, vol. 18, p. 41-49, 2002
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Changani, S.D.; Belmar-Beiny, M.T.; Fryer, P.J. (May 1997). "Engineering and chemical factors associated with fouling and cleaning in milk processing".
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Particles larger than those of colloidal dimensions may also foul e.g., by sedimentation ("sedimentation fouling") or straining in small-size openings.
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The calcium carbonate that forms through this reaction precipitates. Due to the temperature dependence of the reaction, and increasing volatility of CO
303: 4061:"Steam Generator Thermal Performance Degradation Case Studies", Report TR-110018, Electric Power Research Institute, Palo Alto, California, USA, 1998 1639:- kinetic rate constants for the transport, the surface reaction, and the overall deposition reaction, respectively; with the dimension of m/s (when 3200:=0. In the absence of consolidation, the asymptotic fouling is always anticipated by this older model and the fouling progress can be described as: 4172:
H. Mueller-Steinhagen and A.P. Watkinson, "Fouling of Heat Exchanger--New Approaches to Solve Old Problem", Heat Transfer Engineering, 26(2), 2005.
3516: 1939: 3167:{\displaystyle m(t)={{k_{d}C_{m}\rho } \over {\lambda }}\left(t\lambda _{c}+{{\lambda _{r}} \over {\lambda }}\left(1-e^{-\lambda t}\right)\right)} 934:
The following lists some of the industrially common phases of precipitation fouling deposits observed in practice to form from aqueous solutions:
2406:, plants, and animals on surfaces, such as ships and submarine hulls, or piping and reservoirs with untreated water. This can be accompanied by 3358:
station, typical losses could be 20 MW and up (up to 100% if the station shuts down due to fouling-induced component degradation). In seawater
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With time, the resulting surface deposit may harden through processes collectively known as "deposit consolidation" or, colloquially, "aging".
2468:) experienced (presumably) abiotic fouling of solar panels by dust particles from the Martian atmosphere. Some of the deposits subsequently 3828:
Ruckenstein, Eli; Prieve, Dennis C. (1973). "Rate of deposition of Brownian particles under the action of London and double-layer forces".
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Løge, Isaac A.; Bentzon, Jakob R.; Klingaa, Christopher G.; Walther, Jens H.; Anabaraonye, Benaiah U.; Fosbøl, Philip L. (February 2022).
2252:. A maximum fouling rate is usually observed when the fouling particles and the substrate exhibit opposite electrical charge, or near the 4065: 2729:      [ rate of deposit accumulation ] = [ rate of deposition ] - [ rate of re-entrainment of unconsolidated deposit ] 4251: 3339:
input to compensate for the reduced output caused by fouling, and an increased use of cooling water in once-through cooling systems.
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Living organisms – deposition of excess minerals (e.g., calcium, iron, copper) in tissues is (sometimes controversially) linked to
1216: 4102:"Theoretical framework for predicting inorganic fouling in membrane distillation and experimental validation with calcium sulfate" 1865:
An alternative to using the sticking probability is to use a kinetic attachment rate constant, assuming the first order reaction:
4183: 3800: 3206: 1313: 3587: 3327:, premature failure of electrical heating elements, and a large number of other often unanticipated problems. In addition, the 296: 4268: 3709:
Siobhán Francesca E. Boerlage, "Scaling and Particulate Fouling in Membrane Filtration Systems", Taylor & Francis; 2001,
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Induction period, i.e., a near-nil fouling rate at the initial period of fouling (observed only for some fouling mechanisms);
2649:, but may also occur by inertial coasting/impaction, particle interception by the surface (for particles with finite sizes), 2683:
Foulant crystallisation on the surface (or attachment of the colloidal particle, or chemical reaction, or bacterial growth);
2429:), which produce sulfide and often cause corrosion of ferrous metals (and other alloys). Sulfide-oxidizing bacteria (e.g., 2358:
of organic matter. The food industry, for example milk processing, also experiences fouling problems by chemical reactions.
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Fouling phenomena are common and diverse, ranging from fouling of ship hulls, natural surfaces in the marine environment (
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is the accumulation of unwanted material on solid surfaces. The fouling materials can consist of either living organisms (
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in lost revenue in a typical power plant), and the cost of actually doing this maintenance. Finally, fouling is often a
1698:") or in gas progresses by a mechanism different than precipitation fouling. This process is usually most important for 907:
with increasing temperature, the scaling is higher at the hotter outlet of the heat exchanger than at the cooler inlet.
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is also of industrial significance. The particles can be either solid or liquid. The common examples can be fouling by
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Solidification fouling - when components of the flowing fluid with a high-melting point freeze onto a subcooled surface
4287: 122: 3714: 289: 141: 94: 2027: 1871: 927:. Similarly, precipitation fouling can occur because of solubility changes induced by other factors, e.g., liquid 4202:
Herve BODINEAU and Thierry SOLLIER, "Tube support plate clogging up of French steam generators", Eurosafe webpage
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to the fouling curve at zero deposit loading or zero time) and the fouling rate after a long period of time (an
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Bowen, Bruce D; Epstein, Norman (October 1979). "Fine particle deposition in smooth parallel-plate channels".
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and then the transport and attachment kinetic coefficients are combined as two processes occurring in series:
3423:. The generation of the corrosion products in the water piping systems is often minimized by controlling the 3188:
This model reproduces either linear, falling, or asymptotic fouling, depending on the relative values of k, λ
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Chemical reaction fouling, for example, decomposition or polymerization of organic matter on heating surfaces
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phenomenon, this fouling mechanism can be very sensitive to factors that affect colloidal stability, e.g.,
17: 423:– increases pressure drop, increases energy expenditure, reduces flux, membrane failure (in severe cases); 3500: 2641:
Foulant transport from the bulk of the process fluid to the fouling surface. This transport is often by
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are the concentration of the particle foulant at the interface and in the bulk fluid, respectively; kg m.
252: 108: 3583: 3367:-operated coolers is also easily in the two-digit area. In addition to the operational costs, also the 3011:
is the mass loading of the removable (i.e., unconsolidated) fraction of the surface deposit (kg/m); and
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Schematics of the fouling process consisting of simultaneous foulant deposition and deposit removal.
690: 90: 4326: 3546: 3485:. One of the most important unoxidizable biocides is a mixture of chloromethyl-isothiazolinone and 2426: 1642: 75: 3789:
T.R. Bott, "Fouling of Heat Exchangers (Chemical Engineering Monographs)", Elsevier Science, 1995.
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is of primary concern, it is important to note non-uniformity of deposit thickness (e.g., deposit
1741: 2512: 2314:, or fouling of air-cooled components by dust in air. The mechanisms are discussed in article on 1543: 483: 262: 68: 3768: 1584:
for the crystallization reaction and the overall deposition process, respectively, dimensionless
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Examples of components that may be subject to fouling and the corresponding effects of fouling:
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costs should be (but typically are not) considered. The ecological costs arise from the use of
3305: 2719: 2457: 2433:), on the other hand, can produce sulfuric acid, and can be involved in corrosion of concrete. 2389: 893:{\displaystyle {\ce {\mathsf {{Ca(HCO3)2}_{(aqueous)}->{CaCO3(v)}+{CO2}\!{\uparrow }+H2O}}}} 232: 2977:
m is the mass loading of the deposit (consolidated and unconsolidated) on the surface (kg/m);
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for colloidal particles is a function of both the surface chemistry, geometry, and the local
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systems can occur due to differential solubility of barium sulfate in solutions of different
541:. They may also create flow blockages, redistribute the flow inside the components, or cause 35: 4062: 3986:
Hong Lu, "Composite Fouling of Heat Exchanger Surfaces", Nova Science Books, New York, 2007.
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serve as an example of larger animals that have caused widespread fouling in North America.
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can be of particular interest when the impact of fouling on pressure drop is of interest.
8: 4258:", Public Works Technical Bulletin 420-49-34, U.S. Army Corps of Engineers, 15 June 2001. 4100:
Warsinger, David M.; Tow, Emily W.; Swaminathan, Jaichander; Lienhard V, John H. (2017).
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are the kinetic rate constants for deposition and transport, respectively. The value of
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of serious degradation problems that may limit the life of components or entire plants.
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where m is the maximum (asymptotic) mass loading of the deposit on the surface (kg/m).
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also have meanings outside of this scope; therefore, they should be used with caution.
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Kern, D.O.; Seaton, R.E. (1959). "A theoretical analysis of thermal surface fouling".
3930: 3695: 2700:, which account for deposit losing its porosity and becoming more tenacious with time; 931:, liquid degassing, redox potential changes, or mixing of incompatible fluid streams. 657:
Composite fouling, whereby fouling involves more than one foulant or fouling mechanism
4023: 3961: 3876: 3710: 3681: 3559: 3540: 3316: 2712: 2581: 2516: 2504: 2485: 2465: 2430: 2245: 1581: 1538:- equilibrium concentration of the substance at the conditions of the interface, kg/m 938: 928: 753: 367: 347: 331: 207: 176: 115: 3973: 2402:
or biological fouling is the undesirable accumulation of micro-organisms, algae and
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The deposition rate by precipitation is often described by the following equations:
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matter of either biological or inorganic origin, for example industrially produced
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The common particulate fouling deposits formed from aqueous suspensions include:
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with time; plugging; in some cases complete stoppage of flow in a matter of days;
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Løge, Isaac A.; Anabaraonye, Benaiah U.; Fosbøl, Philip Loldrup (October 2022).
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International Convention on the Control of Harmful Anti-fouling Systems on Ships
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the one that is usually more difficult to prevent and therefore more important.
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Generation or ingress of the species that causes fouling ("foulant sourcing");
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in closed systems when sufficient nutrients are present. Examples may include
430:– increases temperature of the element, increases corrosion, reduces lifespan; 4295: 3624: 3489:-isothiazolinone. Also applied are dibrom nitrilopropionamide and quaternary 3470: 3385: 3355: 3351: 3347: 2666: 2607: 2533: 2355: 2295: 2281: 2016:{\displaystyle k_{d}=\left({\frac {1}{k_{a}}}+{\frac {1}{k_{t}}}\right)^{-1}} 534: 456: 343: 339: 267: 4036: 3903: 3586:
alternative. In some heat-transfer applications, mechanical mitigation with
3965: 3494: 3436: 3368: 3359: 2670: 2461: 2436: 2393: 1704: 1036: 635: 452: 437: 2417:, lipids, nucleic acids, etc.). The biofilm structure is usually complex. 4130: 3841: 3591: 2662: 1708: 730: 620: 162: 517:. Such matter enters into the cooling water circuit through the cooling 3432: 3396: 3392: 3328: 2704: 2528: 2399: 2379: 2351: 2269: 1080: 911: 719: 647: 518: 497: 468: 462: 320: 180: 2689:
Deposit dissolution (or re-entrainment of loosely attached particles);
2634:
Foulant transport with the stream of the process fluid (most often by
562:
Tools and other "foreign objects" accidentally left after maintenance;
3512: 3459: 3444: 3443:), control of oxygen dissolved in water (for example, by addition of 3312: 2642: 2635: 2591: 2285: 2273: 1699: 1044: 1040: 1024: 1002: 960: 946: 723: 711: 670: 631: 624: 610: 379: 202: 2627:
Fouling of a system can be modelled as consisting of several steps:
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in airplanes – inaccurate or incorrect indication of airplane speed;
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on teeth or deposits on solar panels on Mars, among other examples.
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This system of equations can be integrated (taking that m = 0 and m
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This article is about fouling in engineering. For uses of the term
2619: 2570:- The fouling rate can be steady with time. This is a common case. 2472:. This illustrates the universal nature of the fouling phenomena. 4099: 3579: 3520: 3482: 3466: 3455: 3428: 3332: 2577: 2403: 2307: 1095: 994: 942: 682: 433: 411: 46: 3594:
cleaning methods are available for many specific applications.
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Corrosion deposits are created in-situ by the corrosion of the
1480:- concentration of the substance in the bulk of the fluid, kg/m 1091: 1032: 1028: 984: 968: 571: 514: 510: 3747:"Spark Plug Faces", brochure "Bosch Spark Plugs 0307", Part 1 3454:
For water systems at relatively low temperatures, the applied
752:- always prevailing in natural water - and the poorly soluble 3943: 3474: 3389: 1695: 1301:{\displaystyle {\frac {dm}{dt}}={k_{r}}(C_{i}-C_{e})^{n_{1}}} 707: 606: 565: 526: 493: 3342:
For example, "normal" fouling at a conventionally fired 500
489:
Teeth – promotes tooth or gum disease, decreases aesthetics;
446:– axial offset anomaly, may need to de-rate the power plant; 362: 169: 154: 3889: 3575: 3567: 3508: 3343: 3336: 3277:{\displaystyle m(t)=m^{*}\left(1-e^{-\lambda _{r}t}\right)} 2956: 2708: 2299: 1396:{\displaystyle {\frac {dm}{dt}}=k_{d}(C_{b}-C_{e})^{n_{2}}} 748:
As an example, the equilibrium between the readily soluble
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barrels - increases chamber pressure; hampers loading for
3916: 3643: 3311:
The losses initially result from impaired heat transfer,
882: 859: 836: 819: 801: 788: 522: 2354:, waxes, etc.). High tube wall temperatures may lead to 417:
Solar panels – decreases the electrical power generated;
3830:
Journal of the Chemical Society, Faraday Transactions 2
3424: 2696:
or differential solubility in temperature gradient) or
1509:- concentration of the substance at the interface, kg/m 813: 807: 791: 775: 414:– reduces efficiency, increases probability of failure; 3299:
Cost relations between the individual types of fouling
3995: 3892:
Comprehensive Reviews in Food Science and Food Safety
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fouling, i.e., accumulation of particles, typically
3427:
of the process fluid (typically alkalinization with
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for the avoidance of biofouling, from the increased
2692:
Deposit consolidation on the surface (e.g., through
1429:- mass of the material (per unit surface area), kg/m 593:
As to micro fouling, distinctions are made between:
2184:
are the kinetic rate constants for deposition, m/s,
2129:
is the rate of the deposition by particles, kg m s,
1204:{\displaystyle {\frac {dm}{dt}}=k_{t}(C_{b}-C_{i})} 459:– inaccurate or incorrect measurement of flow rate; 82:. Unsourced material may be challenged and removed. 27:
Accumulation of unwanted material on solid surfaces
4093: 3276: 3166: 2962: 2232: 2205: 2176: 2121: 2078: 2015: 1922: 1850: 1830: 1803: 1773: 1727: 1677: 1631: 1572: 1530: 1501: 1472: 1443: 1421: 1395: 1300: 1203: 892: 756:, the following chemical equation may be written: 3827: 863: 4293: 3291:Economic and environmental importance of fouling 2997:- mass fraction of foulant in the fluid (kg/kg); 2543: 357: 3946:Critical Reviews in Food Science and Nutrition 408:, increases fuel usage, reduces maximum speed; 2302:and other relatively coarse suspended matter. 2079:{\displaystyle {\frac {dm}{dt}}={k_{d}}C_{b}} 1923:{\displaystyle {\frac {dm}{dt}}={k_{a}}C_{i}} 297: 3854: 3523:, and other "film-forming" amines), organic 3388:and other major industrial installations of 2475: 2333: 737:, the concentration of salts may exceed the 617:(e.g., calcium carbonate or calcium sulfate) 338:components through ingredients contained in 729:Through changes in temperature, or solvent 630:Corrosion fouling, i.e., in-situ growth of 4153: 3004:is the re-entrainment rate constant (1/s); 1694:Fouling by particles suspended in water (" 698:Scaling or precipitation fouling involves 304: 290: 4120: 4013: 3705: 3703: 3671: 3661: 3395:, macro fouling is avoided by way of pre- 3018:is the consolidation rate constant (1/s). 2364: 949:usually at t > ~50 °C, or rarely 885: 873: 850: 827: 810: 779: 770: 142:Learn how and when to remove this message 3857:Journal of Colloid and Interface Science 3315:damage (in particular under-deposit and 3294: 2618: 2383: 689: 681: 665: 661: 373: 361: 168: 153: 38:. For fouling on membrane surfaces, see 3588:dynamic scraped surface heat exchangers 3350:unit accounts for output losses of the 910:In general, the dependence of the salt 366:cross-section of a condenser tube with 14: 4294: 3919:Experimental Thermal and Fluid Science 3785: 3783: 3700: 2987:is the deposition rate constant (m/s); 2408:microbiologically influenced corrosion 1689: 1124:) from extremely pure, low-iron water. 877: 869: 854: 845: 831: 796: 783: 559:Detached internal parts of components; 471:electrodes in cars – engine misfiring; 342:or gases, and even the development of 4037:Mars Pathfinder - Dust Settling (MAE) 3493:compounds. For underwater ship hulls 597:Scaling or precipitation fouling, as 2614: 2442: 2321: 634:deposits, for example, magnetite on 80:adding citations to reliable sources 51: 3780: 2665:(in condensation and evaporation), 378:cross-section of a brass tube with 24: 3511:), long-chain aliphatic amines or 3379: 2451: 2350:or deposition of heavy fractions ( 2270:iron oxides and iron oxyhydroxides 25: 4338: 4276: 3590:is an option. Also ultrasonic or 2392:in Northern France, covered with 2177:{\displaystyle k_{a},k_{t},k_{d}} 1632:{\displaystyle k_{t},k_{r},k_{d}} 686:Extreme boiler pipe scale buildup 3566:, or of low surface energy like 3469:compounds, chlorine and bromide 3354:of 5 MW and more. In a 1,300 MW 2673:(acting on rotating particles), 2122:{\displaystyle {\frac {dm}{dt}}} 588: 504: 404:Ship hulls – creates additional 56: 4261: 4241: 4222: 4213: 4195: 4175: 4166: 4147: 4137: 4084: 4075: 4055: 4041: 4030: 3989: 3980: 3937: 3910: 3883: 3848: 3821: 3620:Steam generator (nuclear power) 580:, parts of plants up to entire 67:needs additional citations for 3812: 3792: 3760: 3741: 3722: 3688: 3637: 3458:may be classified as follows: 3219: 3213: 3045: 3039: 2990:ρ is the fluid density (kg/m); 2950: 2944: 2915: 2909: 2827: 2821: 2306:Fouling by particles from gas 1377: 1350: 1282: 1255: 1198: 1172: 865: 840: 822: 745:of solids (usually crystals). 13: 1: 3931:10.1016/S0894-1777(96)00141-0 3631: 2544:Progress of fouling with time 2373: 2342:. For example, corrosion and 1678:{\displaystyle n_{1}=n_{2}=1} 358:Components subject to fouling 4156:British Chemical Engineering 4122:10.1016/j.memsci.2017.01.031 4002:Chemical Engineering Journal 3958:10.1080/10408398.2012.752343 3877:10.1016/0021-9797(79)90184-X 3650:Chemical Engineering Journal 1774:{\displaystyle k_{d}=Pk_{t}} 7: 4109:Journal of Membrane Science 3597: 3562:(for example, very smooth, 3501:Chemical fouling inhibitors 3026:= 0 at t = 0) to the form: 1573:{\displaystyle n_{1},n_{2}} 533:. In closed circuits, like 521:from sources like the open 509:Macro fouling is caused by 253:Metal-induced embrittlement 10: 4343: 4283:Crude Oil Fouling research 3584:environmentally friendlier 2377: 1213:Surface crystallisation: 1051:Aluminium oxide hydroxides 444:pressurized water reactors 243:Liquid metal embrittlement 44: 29: 4015:10.1016/j.cej.2022.137008 3663:10.1016/j.cej.2021.132583 3610:Oilfield scale inhibition 2521:stress corrosion cracking 2498:heat transfer coefficient 2496:"), or by development of 2476:Quantification of fouling 2470:spontaneously cleaned off 2423:sulfate-reducing bacteria 2334:Chemical reaction fouling 539:heat transfer coefficient 421:Reverse osmosis membranes 258:Stress corrosion cracking 165:, fouled by macro fouling 4249:Magnetic Water Treatment 3547:Magnetic water treatment 2647:turbulent-eddy diffusion 2523:, or localized wastage. 2427:sulfur-reducing bacteria 190:Mechanical failure modes 45:Not to be confused with 34:outside technology, see 3904:10.1111/1541-4337.12000 3481:cleavers, unoxidizable 3346:(net electrical power) 2677:, and other mechanisms. 2458:Mars Exploration Rovers 627:particles, on a surface 263:Sulfide stress cracking 3300: 3278: 3168: 2964: 2624: 2584:to the fouling curve). 2396: 2365:Solidification fouling 2234: 2207: 2178: 2123: 2080: 2017: 1924: 1852: 1832: 1805: 1775: 1729: 1679: 1633: 1574: 1532: 1503: 1474: 1445: 1423: 1397: 1302: 1205: 894: 695: 687: 679: 650:, like settlements of 383: 371: 233:Hydrogen embrittlement 184: 166: 4312:Hydraulic engineering 3298: 3279: 3169: 2965: 2675:thermoelectric effect 2622: 2387: 2235: 2233:{\displaystyle C_{b}} 2208: 2206:{\displaystyle C_{i}} 2179: 2124: 2081: 2018: 1925: 1853: 1833: 1831:{\displaystyle k_{t}} 1806: 1804:{\displaystyle k_{d}} 1776: 1730: 1680: 1634: 1575: 1533: 1531:{\displaystyle C_{e}} 1504: 1502:{\displaystyle C_{i}} 1475: 1473:{\displaystyle C_{b}} 1446: 1424: 1398: 1303: 1206: 895: 722:and often results in 693: 685: 669: 662:Precipitation fouling 377: 365: 172: 157: 36:Foul (disambiguation) 3842:10.1039/F29736901522 3560:Low-fouling surfaces 3449:corrosion inhibitors 3386:steam power stations 3207: 3033: 2742: 2598:Accelerating fouling 2513:intergranular attack 2503:If under-deposit or 2254:point of zero charge 2244:Being essentially a 2217: 2190: 2135: 2096: 2028: 1940: 1872: 1842: 1815: 1788: 1742: 1719: 1713:sticking probability 1643: 1590: 1544: 1515: 1486: 1457: 1435: 1413: 1314: 1217: 1136: 763: 484:petroleum production 476:petroleum reservoirs 76:improve this article 4317:Transport phenomena 3869:1979JCIS...72...81B 3673:20.500.11850/517338 3615:Particle deposition 3564:implanted with ions 3421:ion-exchange resins 3417:electrodeionization 2256:of either of them. 1690:Particulate fouling 991:Magnesium hydroxide 884: 861: 838: 821: 803: 790: 750:calcium bicarbonate 474:Production zone of 393:surfaces – reduces 248:Mechanical overload 4254:2011-12-15 at the 4235:2011-07-10 at the 4207:2011-07-26 at the 4189:2009-05-12 at the 4068:2011-07-10 at the 3806:2009-05-12 at the 3774:2010-05-30 at the 3754:2009-12-29 at the 3735:2006-09-17 at the 3447:), or addition of 3399:and cooling water 3301: 3274: 3164: 2960: 2955: 2625: 2588:Asymptotic fouling 2562:"Negative" fouling 2500:(W/mK) with time. 2494:fouling resistance 2397: 2316:aerosol deposition 2230: 2203: 2174: 2119: 2076: 2013: 1920: 1848: 1828: 1801: 1771: 1725: 1675: 1629: 1570: 1528: 1499: 1470: 1441: 1419: 1393: 1298: 1201: 977:(e.g., beerstone); 890: 872: 849: 826: 778: 773: 768: 696: 688: 680: 395:thermal efficiency 384: 372: 185: 167: 3952:(12): 1724–1743. 3580:complexing agents 3541:process chemicals 3317:crevice corrosion 3125: 3083: 2615:Fouling modelling 2582:oblique asymptote 2505:crevice corrosion 2486:surface roughness 2443:Composite fouling 2431:Acidithiobacillus 2322:Corrosion fouling 2246:surface chemistry 2117: 2049: 1997: 1977: 1893: 1851:{\displaystyle P} 1728:{\displaystyle P} 1582:order of reaction 1444:{\displaystyle t} 1422:{\displaystyle m} 1335: 1238: 1157: 1090:Copper (metallic 939:Calcium carbonate 887: 875: 852: 829: 812: 781: 772: 754:calcium carbonate 368:calcium carbonate 314: 313: 208:Corrosion fatigue 179:with residues of 152: 151: 144: 126: 16:(Redirected from 4334: 4322:Water technology 4271: 4265: 4259: 4245: 4239: 4226: 4220: 4217: 4211: 4199: 4193: 4179: 4173: 4170: 4164: 4163: 4151: 4145: 4141: 4135: 4134: 4124: 4106: 4097: 4091: 4088: 4082: 4079: 4073: 4059: 4053: 4045: 4039: 4034: 4028: 4027: 4017: 3993: 3987: 3984: 3978: 3977: 3941: 3935: 3934: 3914: 3908: 3907: 3887: 3881: 3880: 3852: 3846: 3845: 3825: 3819: 3816: 3810: 3796: 3790: 3787: 3778: 3764: 3758: 3745: 3739: 3726: 3720: 3707: 3698: 3692: 3686: 3685: 3675: 3665: 3641: 3537:polyacrylic acid 3533:polyelectrolytes 3525:phosphonic acids 3505:chelating agents 3441:sodium phosphate 3283: 3281: 3280: 3275: 3273: 3269: 3268: 3267: 3263: 3262: 3234: 3233: 3173: 3171: 3170: 3165: 3163: 3159: 3158: 3154: 3153: 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4256:Wayback Machine 4246: 4242: 4237:Wayback Machine 4227: 4223: 4218: 4214: 4209:Wayback Machine 4200: 4196: 4191:Wayback Machine 4180: 4176: 4171: 4167: 4152: 4148: 4142: 4138: 4104: 4098: 4094: 4089: 4085: 4080: 4076: 4070:Wayback Machine 4060: 4056: 4046: 4042: 4035: 4031: 3994: 3990: 3985: 3981: 3942: 3938: 3915: 3911: 3888: 3884: 3853: 3849: 3826: 3822: 3817: 3813: 3808:Wayback Machine 3797: 3793: 3788: 3781: 3776:Wayback Machine 3765: 3761: 3756:Wayback Machine 3746: 3742: 3737:Wayback Machine 3727: 3723: 3708: 3701: 3693: 3689: 3642: 3638: 3634: 3629: 3600: 3413:reverse osmosis 3405:microfiltration 3382: 3380:Fouling control 3293: 3258: 3254: 3250: 3246: 3239: 3235: 3229: 3225: 3208: 3205: 3204: 3199: 3195: 3191: 3184: 3180: 3142: 3138: 3131: 3127: 3120: 3113: 3109: 3108: 3106: 3097: 3093: 3089: 3085: 3078: 3068: 3064: 3058: 3054: 3053: 3051: 3034: 3031: 3030: 3025: 3017: 3010: 3003: 2996: 2986: 2954: 2953: 2938: 2934: 2925: 2921: 2903: 2899: 2893: 2889: 2877: 2873: 2867: 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121–143. 3882: 3847: 3820: 3811: 3791: 3779: 3759: 3740: 3721: 3718:(Google books) 3699: 3687: 3635: 3633: 3630: 3628: 3627: 3622: 3617: 3612: 3607: 3601: 3599: 3596: 3535:(for example, 3529:etidronic acid 3527:(for example, 3517:octadecylamine 3515:(for example, 3507:(for example, 3401:debris filters 3381: 3378: 3292: 3289: 3285: 3284: 3272: 3266: 3261: 3257: 3253: 3249: 3245: 3242: 3238: 3232: 3228: 3224: 3221: 3218: 3215: 3212: 3197: 3193: 3189: 3182: 3178: 3175: 3174: 3162: 3157: 3151: 3148: 3145: 3141: 3137: 3134: 3130: 3123: 3116: 3112: 3105: 3100: 3096: 3092: 3088: 3081: 3076: 3071: 3067: 3061: 3057: 3050: 3047: 3044: 3041: 3038: 3023: 3020: 3019: 3015: 3012: 3008: 3005: 3001: 2998: 2994: 2991: 2988: 2984: 2981: 2980:t is time (s); 2978: 2971: 2970: 2957: 2952: 2949: 2946: 2941: 2937: 2933: 2928: 2924: 2920: 2917: 2914: 2911: 2906: 2902: 2896: 2892: 2888: 2885: 2880: 2876: 2870: 2866: 2862: 2858: 2855: 2851: 2845: 2841: 2837: 2833: 2832: 2829: 2826: 2823: 2818: 2814: 2808: 2804: 2800: 2797: 2792: 2788: 2782: 2778: 2774: 2770: 2767: 2763: 2759: 2756: 2752: 2751: 2749: 2717: 2716: 2701: 2690: 2687: 2684: 2681: 2678: 2655:thermophoresis 2639: 2632: 2616: 2613: 2612: 2611: 2608:sawtooth curve 2604:Seesaw fouling 2601: 2595: 2585: 2571: 2568:Linear fouling 2565: 2559: 2545: 2542: 2477: 2474: 2453: 2450: 2444: 2441: 2378:Main article: 2375: 2372: 2366: 2363: 2344:polymerization 2335: 2332: 2323: 2320: 2304: 2303: 2293: 2250:zeta potential 2242: 2241: 2227: 2223: 2200: 2196: 2185: 2171: 2167: 2163: 2158: 2154: 2150: 2145: 2141: 2130: 2115: 2112: 2107: 2104: 2087: 2086: 2073: 2069: 2062: 2058: 2053: 2047: 2044: 2039: 2036: 2023: 2010: 2007: 2002: 1994: 1990: 1986: 1981: 1974: 1970: 1966: 1960: 1955: 1950: 1946: 1931: 1930: 1917: 1913: 1906: 1902: 1897: 1891: 1888: 1883: 1880: 1847: 1825: 1821: 1798: 1794: 1782: 1781: 1768: 1764: 1760: 1757: 1752: 1748: 1724: 1691: 1688: 1687: 1686: 1674: 1671: 1666: 1662: 1658: 1653: 1649: 1626: 1622: 1618: 1613: 1609: 1605: 1600: 1596: 1585: 1567: 1563: 1559: 1554: 1550: 1539: 1525: 1521: 1510: 1496: 1492: 1481: 1467: 1463: 1452: 1440: 1430: 1418: 1404: 1403: 1388: 1384: 1379: 1373: 1369: 1365: 1360: 1356: 1352: 1347: 1343: 1339: 1333: 1330: 1325: 1322: 1308: 1293: 1289: 1284: 1278: 1274: 1270: 1265: 1261: 1257: 1251: 1247: 1242: 1236: 1233: 1228: 1225: 1211: 1200: 1195: 1191: 1187: 1182: 1178: 1174: 1169: 1165: 1161: 1155: 1152: 1147: 1144: 1126: 1125: 1121: 1117: 1114:nickel ferrite 1110: 1107:hydroxyapatite 1103: 1088: 1070: 1048: 1006: 988: 981:Barium sulfate 978: 972: 954: 925:ionic strength 904: 901: 900: 879: 871: 867: 856: 847: 842: 833: 824: 815: 809: 798: 793: 785: 777: 735:degasification 676:heat exchanger 663: 660: 659: 658: 655: 645: 642: 639: 628: 618: 590: 587: 586: 585: 575: 569: 563: 560: 557: 553: 552: 550: 535:cooling towers 506: 503: 502: 501: 490: 487: 472: 466: 460: 457:orifice plates 450: 447: 440: 431: 424: 418: 415: 409: 402: 398: 391:Heat exchanger 359: 356: 334:), fouling of 332:marine fouling 312: 311: 309: 308: 301: 294: 286: 283: 282: 281: 280: 275: 270: 265: 260: 255: 250: 245: 240: 235: 230: 225: 220: 215: 210: 205: 200: 192: 191: 159:Heat exchanger 150: 149: 64: 62: 55: 26: 9: 6: 4: 3: 2: 4339: 4328: 4325: 4323: 4320: 4318: 4315: 4313: 4310: 4308: 4305: 4303: 4300: 4299: 4297: 4288: 4286: 4284: 4281: 4280: 4270: 4264: 4257: 4253: 4250: 4244: 4238: 4234: 4231: 4225: 4216: 4210: 4206: 4203: 4198: 4192: 4188: 4185: 4178: 4169: 4162:(5): 258–262. 4161: 4157: 4150: 4140: 4132: 4131:1721.1/107916 4128: 4123: 4118: 4114: 4110: 4103: 4096: 4087: 4078: 4071: 4067: 4064: 4058: 4051: 4044: 4038: 4033: 4025: 4021: 4016: 4011: 4007: 4003: 3999: 3992: 3983: 3975: 3971: 3967: 3963: 3959: 3955: 3951: 3947: 3940: 3932: 3928: 3924: 3920: 3913: 3905: 3901: 3897: 3893: 3886: 3878: 3874: 3870: 3866: 3862: 3858: 3851: 3843: 3839: 3835: 3831: 3824: 3815: 3809: 3805: 3802: 3795: 3786: 3784: 3777: 3773: 3770: 3763: 3757: 3753: 3750: 3744: 3738: 3734: 3731: 3725: 3719: 3716: 3715:90-5809-242-9 3712: 3706: 3704: 3697: 3691: 3683: 3679: 3674: 3669: 3664: 3659: 3655: 3651: 3647: 3640: 3636: 3626: 3625:Tube cleaning 3623: 3621: 3618: 3616: 3613: 3611: 3608: 3606: 3603: 3602: 3595: 3593: 3589: 3585: 3581: 3577: 3571: 3569: 3565: 3561: 3557: 3551: 3548: 3544: 3542: 3538: 3534: 3530: 3526: 3522: 3518: 3514: 3510: 3506: 3502: 3498: 3497:are applied. 3496: 3495:bottom paints 3492: 3488: 3484: 3480: 3476: 3472: 3468: 3464: 3461: 3457: 3452: 3450: 3446: 3442: 3438: 3434: 3430: 3426: 3422: 3418: 3414: 3410: 3406: 3402: 3398: 3394: 3391: 3387: 3377: 3375: 3370: 3366: 3361: 3357: 3356:nuclear power 3353: 3352:steam turbine 3349: 3348:power station 3345: 3340: 3338: 3334: 3330: 3326: 3322: 3318: 3314: 3309: 3307: 3297: 3288: 3270: 3264: 3259: 3255: 3251: 3247: 3243: 3240: 3236: 3230: 3226: 3222: 3216: 3210: 3203: 3202: 3201: 3186: 3160: 3155: 3149: 3146: 3143: 3139: 3135: 3132: 3128: 3121: 3114: 3110: 3103: 3098: 3094: 3090: 3086: 3079: 3074: 3069: 3065: 3059: 3055: 3048: 3042: 3036: 3029: 3028: 3027: 3013: 3006: 2999: 2992: 2989: 2982: 2979: 2976: 2975: 2974: 2947: 2939: 2935: 2931: 2926: 2922: 2918: 2912: 2904: 2900: 2894: 2890: 2886: 2883: 2878: 2874: 2868: 2864: 2860: 2856: 2853: 2849: 2843: 2839: 2835: 2824: 2816: 2812: 2806: 2802: 2798: 2795: 2790: 2786: 2780: 2776: 2772: 2768: 2765: 2761: 2757: 2754: 2747: 2738: 2737: 2736: 2733: 2730: 2727: 2724: 2721: 2714: 2710: 2706: 2702: 2699: 2695: 2691: 2688: 2685: 2682: 2679: 2676: 2672: 2668: 2667:sedimentation 2664: 2660: 2656: 2652: 2648: 2644: 2640: 2637: 2633: 2630: 2629: 2628: 2621: 2609: 2605: 2602: 2599: 2596: 2593: 2589: 2586: 2583: 2579: 2575: 2572: 2569: 2566: 2563: 2560: 2557: 2556: 2552: 2551: 2550: 2541: 2537: 2535: 2534:hot corrosion 2530: 2526: 2522: 2518: 2514: 2510: 2506: 2501: 2499: 2495: 2489: 2487: 2482: 2473: 2471: 2467: 2463: 2459: 2449: 2440: 2438: 2437:Zebra mussels 2434: 2432: 2428: 2424: 2418: 2416: 2411: 2409: 2405: 2401: 2395: 2394:zebra mussels 2391: 2386: 2381: 2371: 2362: 2359: 2357: 2353: 2349: 2345: 2341: 2331: 2329: 2319: 2317: 2313: 2309: 2301: 2297: 2296:Sedimentation 2294: 2291: 2287: 2283: 2282:lepidocrocite 2279: 2275: 2271: 2268: 2267: 2266: 2263: 2260: 2257: 2255: 2251: 2247: 2225: 2221: 2198: 2194: 2186: 2169: 2165: 2161: 2156: 2152: 2148: 2143: 2139: 2131: 2113: 2110: 2105: 2102: 2092: 2091: 2090: 2071: 2067: 2060: 2056: 2051: 2045: 2042: 2037: 2034: 2024: 2008: 2005: 2000: 1992: 1988: 1984: 1979: 1972: 1968: 1964: 1958: 1953: 1948: 1944: 1936: 1935: 1934: 1915: 1911: 1904: 1900: 1895: 1889: 1886: 1881: 1878: 1868: 1867: 1866: 1863: 1861: 1845: 1823: 1819: 1796: 1792: 1766: 1762: 1758: 1755: 1750: 1746: 1738: 1737: 1736: 1722: 1714: 1710: 1706: 1701: 1697: 1672: 1669: 1664: 1660: 1656: 1651: 1647: 1624: 1620: 1616: 1611: 1607: 1603: 1598: 1594: 1586: 1583: 1565: 1561: 1557: 1552: 1548: 1540: 1523: 1519: 1511: 1494: 1490: 1482: 1465: 1461: 1453: 1438: 1431: 1416: 1409: 1408: 1407: 1386: 1382: 1371: 1367: 1363: 1358: 1354: 1345: 1341: 1337: 1331: 1328: 1323: 1320: 1309: 1291: 1287: 1276: 1272: 1268: 1263: 1259: 1249: 1245: 1240: 1234: 1231: 1226: 1223: 1212: 1193: 1189: 1185: 1180: 1176: 1167: 1163: 1159: 1153: 1150: 1145: 1142: 1131: 1130: 1129: 1115: 1112:Magnetite or 1111: 1108: 1104: 1101: 1097: 1093: 1089: 1086: 1082: 1078: 1074: 1071: 1068: 1064: 1060: 1056: 1052: 1049: 1046: 1042: 1038: 1034: 1030: 1026: 1022: 1018: 1014: 1010: 1007: 1004: 1000: 996: 992: 989: 986: 982: 979: 976: 973: 970: 966: 962: 958: 955: 952: 948: 944: 940: 937: 936: 935: 932: 930: 926: 922: 916: 913: 908: 759: 758: 757: 755: 751: 746: 744: 743:precipitation 740: 736: 732: 727: 725: 721: 717: 713: 709: 705: 701: 692: 684: 677: 672: 668: 656: 653: 649: 646: 643: 640: 637: 633: 629: 626: 622: 619: 616: 612: 608: 604: 600: 596: 595: 594: 589:Micro fouling 583: 579: 576: 573: 570: 567: 564: 561: 558: 555: 554: 551: 548: 547: 546: 544: 540: 536: 532: 528: 524: 520: 516: 512: 505:Macro fouling 499: 495: 491: 488: 485: 481: 477: 473: 470: 467: 464: 461: 458: 454: 453:Venturi tubes 451: 448: 445: 441: 439: 438:muzzleloaders 435: 432: 429: 425: 422: 419: 416: 413: 410: 407: 403: 399: 396: 392: 389: 388: 387: 381: 376: 369: 364: 355: 351: 349: 345: 341: 340:cooling water 337: 336:heat-transfer 333: 328: 324: 322: 318: 307: 302: 300: 295: 293: 288: 287: 285: 284: 279: 276: 274: 271: 269: 268:Thermal shock 266: 264: 261: 259: 256: 254: 251: 249: 246: 244: 241: 239: 236: 234: 231: 229: 226: 224: 221: 219: 216: 214: 211: 209: 206: 204: 201: 199: 196: 195: 194: 193: 189: 188: 182: 178: 175: 171: 164: 160: 156: 146: 143: 135: 132:November 2008 124: 121: 117: 114: 110: 107: 103: 100: 96: 93: –  92: 88: 87:Find sources: 81: 77: 71: 70: 65:This article 63: 59: 54: 53: 48: 41: 37: 33: 19: 4263: 4243: 4224: 4215: 4197: 4177: 4168: 4159: 4155: 4149: 4139: 4112: 4108: 4095: 4086: 4077: 4057: 4043: 4032: 4005: 4001: 3991: 3982: 3949: 3945: 3939: 3922: 3918: 3912: 3895: 3891: 3885: 3863:(1): 81–97. 3860: 3856: 3850: 3833: 3829: 3823: 3814: 3794: 3762: 3743: 3724: 3690: 3653: 3649: 3639: 3572: 3552: 3545: 3499: 3453: 3437:ethanolamine 3411:technology ( 3383: 3369:capital cost 3360:desalination 3341: 3310: 3302: 3286: 3187: 3176: 3021: 2972: 2734: 2731: 2728: 2725: 2718: 2709:erosion wear 2671:Magnus force 2626: 2603: 2597: 2587: 2573: 2567: 2561: 2553: 2547: 2538: 2529:permeability 2502: 2490: 2483: 2479: 2455: 2448:components. 2446: 2435: 2419: 2412: 2398: 2368: 2360: 2337: 2325: 2305: 2264: 2261: 2258: 2243: 2088: 1932: 1864: 1862:conditions. 1783: 1705:flocculation 1693: 1405: 1132:Transport: 1127: 1105:Phosphates ( 1037:cristobalite 1027:, amorphous 933: 917: 909: 902: 747: 728: 697: 636:carbon steel 592: 508: 482:– decreased 385: 352: 329: 325: 316: 315: 222: 138: 129: 119: 112: 105: 98: 86: 74:Please help 69:verification 66: 31: 18:Lead fouling 4115:: 381–390. 3177:where λ = λ 2713:exfoliation 2698:cementation 2663:Stefan flow 2466:Opportunity 2356:carbonizing 2352:asphaltenes 2298:fouling by 1709:coagulation 965:hemihydrate 731:evaporation 621:Particulate 613:from water 519:water pumps 463:Pitot tubes 426:Electrical 163:power plant 161:in a steam 4296:Categories 4269:(abstract) 4230:(abstract) 4063:(abstract) 4008:: 137008. 3656:: 132583. 3632:References 3513:polyamines 3433:morpholine 3397:filtration 3393:technology 3374:root cause 3365:compressor 3329:ecological 2720:Deposition 2400:Biofouling 2390:canal lock 2380:Biofouling 2374:Biofouling 2312:flue gases 1310:Overall: 1081:cancrinite 1013:serpentine 912:solubility 739:saturation 720:hard water 712:hydroxides 648:Biofouling 611:hydroxides 498:senescence 469:Spark plug 321:biofouling 183:(cut open) 181:biofouling 102:newspapers 4024:249223220 3682:240007081 3460:inorganic 3445:hydrazine 3313:corrosion 3256:λ 3252:− 3244:− 3231:∗ 3147:λ 3144:− 3136:− 3122:λ 3111:λ 3095:λ 3080:λ 3075:ρ 2932:⋅ 2923:λ 2919:− 2891:λ 2887:− 2884:ρ 2803:λ 2799:− 2796:ρ 2643:molecular 2636:advection 2592:asymptote 2328:substrate 2286:maghemite 2274:magnetite 2006:− 1700:colloidal 1451:- time, s 1364:− 1269:− 1186:− 1045:xonotlite 1041:pectolite 1025:gehlenite 1009:Silicates 1003:periclase 961:anhydrite 947:aragonite 866:↑ 841:↓ 823:⟶ 724:limescale 716:solutions 702:of solid 671:Limescale 654:and algae 632:corrosion 625:colloidal 615:solutions 601:of solid 480:oil wells 401:blockage; 380:corrosion 203:Corrosion 174:Condenser 91:"Fouling" 4252:Archived 4233:Archived 4205:Archived 4187:Archived 4066:Archived 3974:32303762 3966:24731003 3836:: 1522. 3804:Archived 3772:Archived 3752:Archived 3733:Archived 3598:See also 3592:abrasive 3556:Blowdown 3491:ammonium 3483:biocides 3471:cleavers 3463:chlorine 3456:biocides 3409:membrane 3333:biocides 3325:fretting 2705:spalling 2703:Deposit 2525:Porosity 2509:waviness 2340:catalyst 2308:aerosols 2290:goethite 2278:hematite 1100:tenorite 1085:noselite 1077:analcite 1067:corundum 1063:diaspore 1059:gibbsite 1055:boehmite 1021:gyrolite 951:vaterite 929:flashing 652:bacteria 638:surfaces 549:Examples 545:damage. 543:fretting 412:Turbines 348:calculus 278:Yielding 228:Fracture 198:Buckling 4307:Filters 4302:Fouling 3865:Bibcode 3521:helamin 3467:bromide 3429:ammonia 3321:fatigue 3192:, and λ 2973:where: 2578:tangent 2517:pitting 2410:(MIC). 2404:diatoms 2348:olefins 2089:where: 1406:where: 1096:cuprite 995:brucite 943:calcite 811:aqueous 572:Mussels 434:Firearm 370:scaling 317:Fouling 223:Fouling 218:Fatigue 116:scholar 47:fowling 4144:12171. 4022:  3972:  3964:  3713:  3680:  3568:Teflon 3531:), or 3487:methyl 3479:oxygen 2462:Spirit 1784:where 1092:copper 1033:quartz 1029:silica 1017:acmite 985:barite 969:gypsum 710:, and 708:oxides 609:, and 607:oxides 582:trunks 578:Leaves 527:rivers 515:refuse 511:coarse 382:traces 344:plaque 238:Impact 118:  111:  104:  97:  89:  4184:(pdf) 4105:(PDF) 4050:(pdf) 4020:S2CID 3970:S2CID 3801:(pdf) 3769:(pdf) 3749:(pdf) 3730:(pdf) 3696:(pdf) 3678:S2CID 3576:acids 3475:ozone 3419:) or 3390:water 2711:, or 2456:NASA 1116:(NiFe 714:from 704:salts 603:salts 566:Algae 531:lakes 494:aging 213:Creep 123:JSTOR 109:books 3962:PMID 3711:ISBN 3578:and 3509:EDTA 3477:and 3465:and 3337:fuel 2527:and 2464:and 2425:(or 2300:silt 2213:and 1811:and 1696:crud 828:CaCO 478:and 406:drag 273:Wear 177:tube 95:news 32:foul 4127:hdl 4117:doi 4113:528 4010:doi 4006:446 3954:doi 3927:doi 3900:doi 3873:doi 3838:doi 3668:hdl 3658:doi 3654:430 3439:or 3323:), 3306:GDP 3181:+ λ 2645:or 2536:). 1715:", 1707:or 997:); 919:in 780:HCO 733:or 529:or 523:sea 346:or 78:by 4298:: 4158:. 4125:. 4111:. 4107:. 4018:. 4004:. 4000:. 3968:. 3960:. 3950:55 3948:. 3923:14 3921:. 3896:12 3894:. 3871:. 3861:72 3859:. 3834:69 3832:. 3782:^ 3702:^ 3676:. 3666:. 3652:. 3648:. 3543:. 3519:, 3473:, 3451:. 3435:, 3431:, 3425:pH 3415:, 3407:, 3344:MW 3185:. 2707:, 2669:, 2661:, 2657:, 2653:, 2638:); 2519:, 2515:, 2318:. 2292:); 2288:, 2284:, 2280:, 2276:, 1735:: 1580:- 1109:); 1102:); 1098:, 1094:, 1087:); 1083:, 1079:, 1069:); 1065:, 1061:, 1057:, 1047:); 1043:, 1039:, 1035:, 1031:, 1023:, 1019:, 1015:, 1005:); 987:); 971:); 967:, 963:, 953:); 945:, 851:CO 771:Ca 726:. 706:, 605:, 525:, 455:, 4247:" 4160:4 4133:. 4129:: 4119:: 4072:. 4052:. 4048:( 4026:. 4012:: 3976:. 3956:: 3933:. 3929:: 3906:. 3902:: 3879:. 3875:: 3867:: 3844:. 3840:: 3684:. 3670:: 3660:: 3271:) 3265:t 3260:r 3248:e 3241:1 3237:( 3227:m 3223:= 3220:) 3217:t 3214:( 3211:m 3198:c 3194:c 3190:r 3183:c 3179:r 3161:) 3156:) 3150:t 3140:e 3133:1 3129:( 3115:r 3104:+ 3099:c 3091:t 3087:( 3070:m 3066:C 3060:d 3056:k 3049:= 3046:) 3043:t 3040:( 3037:m 3024:r 3016:c 3014:λ 3009:r 3007:m 3002:r 3000:λ 2995:m 2993:C 2985:d 2983:k 2951:) 2948:t 2945:( 2940:r 2936:m 2927:c 2916:) 2913:t 2910:( 2905:r 2901:m 2895:r 2879:m 2875:C 2869:d 2865:k 2861:= 2857:t 2854:d 2850:/ 2844:r 2840:m 2836:d 2828:) 2825:t 2822:( 2817:r 2813:m 2807:r 2791:m 2787:C 2781:d 2777:k 2773:= 2769:t 2766:d 2762:/ 2758:m 2755:d 2748:{ 2715:. 2492:" 2460:( 2272:( 2226:b 2222:C 2199:i 2195:C 2170:d 2166:k 2162:, 2157:t 2153:k 2149:, 2144:a 2140:k 2114:t 2111:d 2106:m 2103:d 2072:b 2068:C 2061:d 2057:k 2052:= 2046:t 2043:d 2038:m 2035:d 2009:1 2001:) 1993:t 1989:k 1985:1 1980:+ 1973:a 1969:k 1965:1 1959:( 1954:= 1949:d 1945:k 1916:i 1912:C 1905:a 1901:k 1896:= 1890:t 1887:d 1882:m 1879:d 1846:P 1824:t 1820:k 1797:d 1793:k 1767:t 1763:k 1759:P 1756:= 1751:d 1747:k 1723:P 1685:) 1673:1 1670:= 1665:2 1661:n 1657:= 1652:1 1648:n 1625:d 1621:k 1617:, 1612:r 1608:k 1604:, 1599:t 1595:k 1566:2 1562:n 1558:, 1553:1 1549:n 1524:e 1520:C 1495:i 1491:C 1466:b 1462:C 1439:t 1417:m 1387:2 1383:n 1378:) 1372:e 1368:C 1359:b 1355:C 1351:( 1346:d 1342:k 1338:= 1332:t 1329:d 1324:m 1321:d 1292:1 1288:n 1283:) 1277:e 1273:C 1264:i 1260:C 1256:( 1250:r 1246:k 1241:= 1235:t 1232:d 1227:m 1224:d 1199:) 1194:i 1190:C 1181:b 1177:C 1173:( 1168:t 1164:k 1160:= 1154:t 1151:d 1146:m 1143:d 1122:4 1120:O 1118:2 1075:( 1053:( 1011:( 1001:( 993:( 983:( 959:( 941:( 905:2 886:O 878:2 874:H 870:+ 855:2 846:+ 832:3 814:) 808:( 797:2 792:) 784:3 776:( 678:. 584:. 574:; 568:; 500:. 496:/ 305:e 298:t 291:v 145:) 139:( 134:) 130:( 120:· 113:· 106:· 99:· 72:. 49:. 42:. 20:)

Index

Lead fouling
Foul (disambiguation)
Membrane fouling
fowling

verification
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"Fouling"
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JSTOR
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Heat exchanger
power plant

Condenser
tube
biofouling
Buckling
Corrosion
Corrosion fatigue
Creep
Fatigue
Fouling
Fracture
Hydrogen embrittlement

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