Fouling, or corrosion product deposition, plagues numerous fields of energy production. At its core is adhesion between dissimilar materials. Understanding and controlling adhesion could reduce or eliminate fouling. This paper demonstrates pool boiling experiments (macroscale) and atomic force microscope force-spectroscopy measurements (microscale), which when in agreement, indicate fouling-resistance.
The buildup of fouling deposits in energy systems degrades their ability to transfer heat, reducing efficiency and causing operational issues such as localized corrosion. Each application presents its own challenges. In nuclear power generation, the buildup of CRUD (Chalk River Unidentified Deposits) induces unique, negative effects ranging from reduced heat transfer, to axial power shifting, to CRUD-induced localized corrosion (CILC), the last of which can cause sudden fuel failure. Knowledge of why CRUD forms and how to prevent its adhesion to nuclear fuel rods represents a major step towards eliminating it. This paper demonstrates a methodology to ascertain which materials may resist CRUD adhesion, thereby preventing its initiation and growth. It presents experiments targeted at multiple length scales: pool boiling (macroscale), which simulates CRUD initiation processes in a nuclear reactor, and atomic force microscope (AFM) force spectroscopy (microscale), which yields quantitative measurements of the adhesion between CRUD constituents and candidate CRUD-resistant materials. Early data from both sets of experiments show some correlation, suggesting that AFM force spectroscopy (AFM-FS) may be used to pre-screen materials for fouling resistance. So far, it appears that CRUD constituents adhere well to oxides, while carbides show both greatly reduced adhesion and no adherent CRUD in pool boiling experiments. The relationship between the AFM-FS measurements and the growth of CRUD in the pool boiling experiments may provide insight into the possible factors affecting fouling in nuclear reactors, eventually leading to its elimination.
Fouling, or the unwanted buildup of corrosion products on a surface, complements corrosion as a surface-based material degradation mechanism. Fouling is particularly detrimental in energy systems, as the surfaces which transfer the most enthalpy are typically the most susceptible. In essence, the presence of fouling deposits, often porous and/or thermally insulating, impedes the efficient flow of heat through a system. The high flow rates and large temperature differences in the hot and cold sections of a heat transfer system or coolant loop provide ideal environments to induce flow-assisted corrosion, and subsequent transport of corrosion products from areas producing soluble & particulate species, to the areas in which deposition is most favorable. In most energy systems, corrosion is most severe in the hottest sections of a coolant loop, since corrosion rates often accelerate exponentially with temperature. In the case of systems undergoing boiling, however, the formation and cavitation of bubbles on a material surface may induce species precipitation via microlayer dryout underneath bubbles. Here the growth of fouling deposits can be particularly rapid, and the resultant effects unusually devastating. Economically, heat exchanger fouling costs many industrial countries roughly 0.25% of its gross domestic product in annual lost productivity due to fluid treatment, cleaning, component replacement, and loss of production 1, equivalent to approximately $42 billion in the United States. Figures for worldwide industries such as boilers, marine shipping, and oil/gas production are far higher.
In nuclear light water reactors (LWRs), foulants composed of soluble and particulate nickel- and iron-bearing species deposit on fuel cladding rods to form CRUD, or Chalk River Unidentified Deposits. CRUD takes the form of highly porous deposits roughly tens to one hundred microns thick, with porosities on the order of 50%. In pressurized water reactors (PWRs), CRUD is largely formed from deposits of nickel ferrites (NixFe3−xO4) in addition to small amounts of NiO, Ni metal, and some iron and nickel chromites (FeCr2O4, NiCr2O4, and NixFe1−xCr2O4) 1,19. Images of CRUD at different length scales are shown in Figure 1. 2 It takes the form of brownish-grey deposits on fuel rods, which when viewed in cross section exhibits multiple, self-similar length scales of porosity. The larger pores, known as "boiling chimneys," provide a path for vaporized water to escape the CRUD, while the smaller pores throughout serve to draw water within. This porous network of CRUD normally draws water into its pores via capillary action, but dryout may occur for very high values of heat flux. The smallest constituents of CRUD are particles, some crystalline, of the iron-nickel-chromium oxides which form the nanoporous framework. Zinc oxides and zirconium oxide are also sometimes present in CRUD.
CRUD can cause multiple negative side effects in PWRs, including CRUD-induced localized corrosion (CILC), which can lead to sudden fuel failure, elevated cladding temperatures due to CRUD's additional thermal resistance, and downward axial power shifts in the reactor 9. Previous studies 3 have shown that Zircaloys (of which PWR fuel cladding is made) corrode far more quickly at elevated temperatures. Recent multiphysics modeling efforts 4 have shown that the presence of CRUD tens of microns thick can elevate cladding temperatures by 15°C, which corresponds to roughly a doubling of the corrosion rate. The last problem of axial power shifting is due to the accumulation of boron, present to control the neutron population in the reactor, in the pores of the CRUD. Recent massively parallel, multiphysics simulations of CRUD's effects 5 demonstrated this effect by simulating CRUD formation and boron accumulation along 3,000 fuel rods in a reactor, demonstrating a downward shift in reactor power. This behavior was already known from nuclear plant measurements 6.
Previous attempts have been made to develop materials resistant to CRUD formation. Solutions have included manipulating the growth of CRUD to improve heat transfer 10, manipulating water chemistry to minimize CRUD growth and corrosion 11, pretreating zircaloy 12, and using magnetic separation as a filtration system 21. One recent patent 7 proposed to electropolish fuel cladding surfaces, to remove nucleation sites for bubbles which can induce CRUD. However, so far no method has resulted in completely preventing the growth of CRUD. We believe that uncovering the mechanism of the initiation event of CRUD formation, the adhesion of the first particles to a substrate, is the key to preventing its formation altogether. Therefore, precise measurement of surface adhesion forces, along with proof-of-principle experiments at higher length scales, is required to predict and confirm the fouling resistance of candidate materials.
This paper presents an experimental, multiscale methodology to discover materials that can be applied to nuclear fuel cladding and prevent the growth of CRUD. In order to achieve this goal, a variety of materials are being tested, shown in Table 1, representing different classes of potential anti-fouling and model materials. First, sputtered or grown specimens of each material are exposed an environment similar to that of a nuclear reactor, specifically a PWR (Pressurized Water Reactor), and "cooked," or indirectly heated to induce pool boiling with excess amount of CRUD forming particulates (NiO and Fe3O4) to simulate the boiling process on the surfaces of nuclear fuel rods. The cooked samples containing simulated CRUD are then imaged top-down using a high-resolution scanning electron microscope (SEM) and in cross section using a focused ion beam (FIB), allowing for visualization of any CRUD-substrate bond that may be present.
The experimental pool boiling setup that has been developed possesses certain unique benefits that make experiments repeatable, effective, and more representative of in-reactor conditions. A vertically oriented sample holder, as shown in Figure 2 prevents nickel- and iron-based particulates that fall out of solution from depositing on the surface of the sample by gravity. Strongly sonicating the CRUD-bearing solution prior to the experiment allows for longer test times and less precipitation of particulates. In addition, for each of the four samples being tested, the heat flux and temperature is recorded throughout the experiment. The pH of the simulated PWR water is also recorded throughout the experiment.
In order to quantify the bond between the CRUD deposits and the surface, we also perform AFM force spectroscopy (AFM-FS) measurements in both air and simulated PWR water on clean surfaces of the same materials. First, AFM cantilevers are functionalized with particles made of one micron spheres of compounds commonly found in CRUD (NiO or Fe3O4). In the MFP3D-BIO, the AFM used in this procedure, the cantilever is modeled so that the force applied to the cantilever tip is proportional to its deflection when in contact with the surface. A laser reflects off the cantilever to a photodetector to measure its deflection. In the procedure below, two constants, the spring constant and the deflection InvOLS (inverse optical lever sensitivity) must be calibrated in order to convert the deflection read by the photodetector to nanoNewtons.
In order to record adhesion of the tip to the surface, the cantilever tip is pressed against the surface of the sample with a force of 25nN. In the experiments recorded below, the tip will then remain at the surface for a period of either 0, 5, 10, 30, or 60 seconds. As the cantilever is being retracted, the tip will often adhere to the sample surface, causing the cantilever to deflect until the force of the cantilever deflection is greater than the adhesion between the CRUD particle and the surface under investigation. Then the cantilever snaps back to zero deflection. It is this maximum deflection, and its corresponding adhesion force, that the AFM can quickly and repetitively record 18. The area under the force-distance curve produced by AFM-FS is a direct measure of the work of separation between CRUD and a substrate, and therefore quantitatively estimates the adhesion of that CRUD particle to each surface. Using the same AFM cantilever on multiple samples eliminates variability in particulate size and composition.
This unique combination of simulated CRUD growth and AFM measurements provides multiple, coupled datasets that allow us to understand how and why CRUD may develop on certain material surfaces. Rather than undergo time-consuming pool boiling experiments, which can take up to a day to complete, a large number of materials can be pre-screened using AFM-FS to estimate their fouling resistance. We also show initial results confirming the efficacy of this procedure, whereby materials which exhibit little to no CRUD adhesion in pool boiling also show very low values of CRUD-substrate adhesion in AFM-FS. Conversely, materials which grow large amounts of adherent CRUD in pool boiling also adhere strongly to CRUD particles in the AFM.
1. Material Preparation
2. Cooking sample
3. Cooking Preparation
4. Cooking
5. Clean-up
6. Atomic Force Microscopy Force Spectroscopy in PWR Water
7. Clean Up
Initial results show that experiments in both the pool boiling facility and the AFM-FS measurements show some correspondence. Materials which grew visually adherent CRUD in pool boiling exhibited high values of adhesion in AFM-FS, while materials on which CRUD did not grow exhibit low values of adhesion in AFM-FS. In addition, the average adhesion force vs. dwell time increased for materials on which CRUD grew, while potential CRUD-resistant materials did not exhibit this increase.
Section 1.1: SEM/FIB Images
Figure 5 shows an SEM image from the FIB of CRUD grown on a sample of TiO2, cooked in the experimental facility shown similar to Figure 2, except the sample was oriented horizontally, and there was only one sample in the chamber rather than four. This image clearly shows adherence between the simulated CRUD and the TiO2 substrate. Figure 6 shows an image of a sample of CRUD-like particles deposited on ZrC. This image shows the limited bonding between the ZrC and the CRUD. In particular, one should notice that the CRUD on TiO2 is strongly adherent to the substrate, leaving no porosity between CRUD and TiO2. By contrast, the CRUD particles on ZrC are clearly not adhered to the substrate, rather they simply sit on the exposed surface. No adhered CRUD particles were present on this sample. The horizontal orientation of the sample surfaces presented in this paper explains the presence of large pieces of CRUD that are sitting on but not adhered to the surface of the sample. These particles likely deposited from the simulated PWR water with nanoparticles clustering and settling out of solution, without adhesion. During the experiment, CRUD particles can come out of PWR solution and drift down to the sample surface when the sample is horizontally oriented. The vertical orientation should eliminate this problem. Figure 7 shows evidence that the larger sediments on the sample surface are not adhered to the surface, as an omniprobe in the FIB easily moved them with a little prodding.
Section 1.2: AFM-FS Measurements
Figure 8 shows a single sample force curve 13. The x-axis reflects the tip distance from the surface of the sample, and the y-axis records the force felt by the tip, which is proportional to the deflection of the cantilever. A positive force corresponds to the tip being pushed by the sample surface and a negative force to the tip being pulled by the sample surface, but still held on by adhesion forces. The black line records the approach, while the red line records the retraction of the sample from the surface. This graph also presents effects of electrostatic forces as the sample approaches. Particularly for the AFM tips with NiO in air, electrostatic forces had a significant effect on the force during the approach, causing significant deflection away from (negative force) or towards the sample surface (positive force) until it contacted the surface. Therefore, data using Fe3O4 functionalized AFM cantilevers will be presented in this section, as these electrostatic effects were not observed as strongly. The adhesion data recorded is the difference between zero deflection, and the minimum force felt by the cantilever.
Figures 9 and 11 present the AFM-FS in-air data based on dwell time at the surface for TiO2 and ZrC surfaces with Fe3O4 tips. For TiO2, average adhesion increases with increasing dwell time, while the ZrC presents the opposite result. In addition, the measured adhesion forces, in both air and water, are visibly greater for TiO2. Figures 10 and 12 present similar data, but performed in a droplet of simulated PWR water. Here, the average adhesion of the ZrC is also consistently less than in adhesion of the TiO2. It is important to note the change of scale on the y-axis and the significant decrease in adhesion force between air and water. All AFM data points, except those with a dwell time of 60 seconds are the average of 36 adhesion measurements. Data points with dwell times of 60 seconds are the average of 16 adhesion measurements.
LWR Materials | Model Materials | New Materials | Geometric Mods |
Au | Tetragonal ZrO2 | ||
Ag | Monoclinic ZrO2 | Nucleation sites | |
Native Zircaloy-4 | SiO2 | ZrN | Micropillars |
100nm ZrO2 | Al2O3 | ZrC | Hydrophobic coatings |
2μm ZrO2 | MgO | ZrB2 | Hydrophilic coatings |
Diamond-like carbon (DLC) | Ti-equivalents (TiN, TiC, TiB2) | Biphilic coatings | |
Graphene | CeO2 |
Table 1: Materials and surface modifications considered in this study. Materials referred to in this study are shown in bold.
Figure 1: Multiscale Images of CRUD in PWRs 2, showing (a) Appearance of CRUD on fuel cladding rods as a brownish deposit layer (b) Microporous CRUD structure showing boiling chimneys (dark) and porous structure, and (c) Examples of CRUD crystalline particulate constituents. Please click here to view a larger version of this figure.
Figure 2: Pool Boiling Experimental Facility Diagram. Please click here to view a larger version of this figure.
Figure 3: Pool Boiling Facility Control Box Diagram. Please click here to view a larger version of this figure.
Figure 4: Thermocouple Amplification Circuit Diagram. Please click here to view a larger version of this figure.
Figure 5: SEM/FIB Image of CRUD Growth on TiO2, 20,000x & 150,000x. Please click here to view a larger version of this figure.
Figure 6: SEM/FIB Image of CRUD Growth on ZrC, 5,000x. Please click here to view a larger version of this figure.
Figure 7: SEM/FIB Image of CRUD. These images show an Omni Probe in the FIB rolling a large piece of CRUD that had deposited, but not adhered to the surface. Please click here to view a larger version of this figure.
Figure 8: Example AFM-FS Single Force Curve 13. The black curve represents loading, while the red curve represents unloading. The green area gives a quantitative estimate of adhesion energy. Please click here to view a larger version of this figure.
Figure 9: AFM-FS measurement of the adhesion of Fe3O4 tip to TiO2 in Air. Data are averages of 36 measurements at times of 0-30 s dwell time, and 16 measurements at times of 60 s. Error bars show the minimum and maximum of all measurements taken at each dwell time. Please click here to view a larger version of this figure.
Figure 10: AFM-FS measurement of the adhesion of Fe3O4 tip to TiO2 in Water. Data are averages of 36 measurements at times of 0-30 s dwell time, and 16 measurements at times of 60 s. Error bars show the minimum and maximum of all measurements taken at each dwell time. Please click here to view a larger version of this figure.
Figure 11: AFM-FS measurement of the adhesion of Fe3O4 tip to ZrC in Air. Data are averages of 36 measurements at times of 0-30 s dwell time, and 16 measurements at times of 60 s. Error bars show the minimum and maximum of all measurements taken at each dwell time. Please click here to view a larger version of this figure.
Figure 12: AFM-FS measurement of the adhesion of Fe3O4 tip to ZrC in Water. Data are averages of 36 measurements at times of 0-30 s dwell time, and 16 measurements at times of 60 s. Error bars show the minimum and maximum of all measurements taken at each dwell time. Please click here to view a larger version of this figure.
This facility has several features that will produce reliable and useful results. First, the vertical orientation of the sample surface prevents solution precipitates from depositing on the surface, as was observed in Figures 5-6. Particularly important are the heat flux sensors, used to directly measure heat flux by differences in thermocouple height vs. temperature, rather than back-calculating a heat flux just from temperature measurements. This helps to further ensure experimental repeatability. Finally, the small water circulation pump prevents film boiling from occurring and promotes sub-cooled nucleate boiling, which is the true condition under which CRUD develops in reactors. Sonicating the simulated PWR water also prevents particles from falling out of solution during boiling. Once again, while this facility is specialized to work with CRUD, many of its traits could be used in other fouling growth experiments. The use of the small amplifying circuit in Figure 4 and a credit-card sized datalogger is a small, simple feature that is applicable for any experiment that collects data electronically, replacing an entire computer and monitor with a circuit board the size of a credit card.
The use of AFM for force spectroscopy can provide repeatable experimental data of adhesion between varieties of dissimilar materials quickly and efficiently. In the procedure shown here, the AFM is outfitted with a tip specifically suited for our research needs. While this procedure is applied to the adhesion of CRUD on a sample, with a variability of tip sizes, shapes, and materials, the procedure shown here is applicable to any problem where the adhesion between two materials at the atomic level in air or in any optically transparent fluid may be useful. AFM-FS has already been used to quantify adhesion and debonding forces between cells 14, organic molecules on glass 15, and between dissimilar solids 16.
For each installation of the chip with the cantilever and tip, the deflection InvOLS and the spring constant will be slightly different, in part because of slight differences in how it is mounted, and in part because the ambient humidity and temperature may also have changed. Recent experimentally validated models have quantified the change in adhesion of AFM-FS measurements as a function of humidity and surface/tip compositions 17. However, with the ability of the AFM to complete large numbers of measurements quickly, statistically significant results can easily be ascertained.
Figures 9-12 all show a significant decrease in adhesion measurements from air to water. This is to be expected as the decrease of AFM measurements in water with respect to air is a well-documented phenomenon 22. The presence of conductive water, which contains H3BO3 and LiOH, likely eliminates any electrostatic forces present in the AFM-FS in-air measurements. The in-water data also represent conditions more realistic to those found in a PWR. Even so, the data in air and in water show relative correspondence, even though the absolute magnitudes of the in-water data are lower. Because these measurements represent the critical, quantitative data in this procedure, proper measurement techniques in Step 6 are critical to acquiring the data in this procedure. In particular, calibrating the individual spring constants of each tip, in air and in water, represent the largest potential sources of experimental error, and should not be omitted.
Looking at the results from the AFM and the FIB together, it is clear that the adhesion force is likely a significant factor in the growth of CRUD on each substrate. In both air and simulated PWR water, the TiO2 AFM-FS measurements are consistently higher than those on ZrC. In Figure 5, the CRUD is tightly bound to the TiO2 substrate, while in Figure 6, the CRUD sits on a few nanoparticles that appear to rest on the surface of the ZrC substrate, creating a far weaker bond if any at all. These preliminary data suggest that the AFM-FS measurements can predict relative bond strength of CRUD, or any fouling deposit, to candidate anti-fouling substrates. Here, the AFM-FS results have been corroborated by simulated growth of CRUD. The AFM-FS measurements can be extremely useful in providing an initial screening test for coatings or surface modifications that can limit CRUD growth in nuclear reactors. While this method of AFM measurement and accelerated fouling growth is used here for fouling in nuclear reactors, it can be easily applied to find protective coatings for fouling in many other applications, or to find a substrate the will promote growth of a mineral or crystal.
The authors have nothing to disclose.
The authors gratefully acknowledge funding by the Electric Power Research Institute (EPRI)'s PWR Technical Advisory Committee (P-TAC), under grant number 00-10001674. The authors also gratefully acknowledge a donation of Zircaloy-4 material by ATI Wah-Chang, Inc.
Atomic Force Microscope | Asylum | MFP3D-BIO | |
AFM Functionalized Cantilevers | Novascan | 1 micron spheres glued on using proprietary technique | |
NiO Nanoparticles | Alfa Aesar | 8-20nm average particle size | |
Fe3O4 Nanoparticles | Alfa Aesar | 20-30mn average particle size | |
Silver conductive grease with silicone base | Chemtronics | The higher the thernal conductivity, the better | |
H3BO3 | Mallinckrodt | 99.945% pure | |
LiOH | Alfa Aesar | 99.995% pure | |
Heat Flux Sensor (500kW/m2) | Captec Enterprise | 1cm x 1cm | |
PID Temperature Controller | Omega | C9000A | Configured for SSR operation |
Logomatic V2 Serial Data Logger in Enclosure | Ocean Controls | Acquires 0-3.3V, 0-12V, or 4-20mA signals on 8 channels at up to 1kHz |
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