ITI Logo Northwestern University Northwestern University
ITI  Northwestern
ITI Home Page ITI Home Page
Home About Us Research Technology Transfer Education Management & Policy Resources Contact Us
Overview
Activities
Autonomous Crack Measurement (ACM)
Infrastructure Inquiries
Knowledge Services
Listservs
Midwest Bridge Group
Publications
Time Domain Reflectometry (TDR)
Topical Bibliographies
Videos
 

Issues Impacting Bridge Painting: an Overview
FHWA/RD/94/098 –August 1995

Abstract | Table of Contents | Executive Summary | Chapter 1 | Chapter 2 | Chapter 3 | Chapter 4 | Chapter 5 | Chapter 6 | Chapter 7 | Appendix A | References | List of Figures | List of Tables

Chapter 3. Task B - Worker Protection/Paint Removal

Table of Contents

INTRODUCTION

The objective of task B was to review current worker health and safety practices pertaining to the removal of lead-based paint from existing structures. This included reviewing containment concepts and methods of testing the relative efficiency and safety of different types of paint-removal methods. Development of a test chamber to assess the relative merits of various removal techniques also was suggested in the initial plan. The objectives were achieved by: (1) assessing information obtained from state and federal DOT personnel, the general literature (including Steel Structure Painting Council (SSPC) publications), and materials and equipment suppliers, (2) conducting and participating in field paint removal and recoating trials, (3) observation and assessment of contract bridge repainting operations done in cooperation with State departments of transportation, especially the Illinois Department of Transportation (IDOT), and (4), performing laboratory tests and analysis of samples from the various field operations in addition to samples prepared in the laboratory.

The program plans were reviewed with an advisory committee consisting of experts in the field, including State DOT representatives from Oregon, Illinois, and Kentucky; the Army Corps of Engineers; paint and thermal spray companies; and the FHWA program monitor. The general consensus of the committee was that it would be difficult to develop and qualify a universal test chamber to accurately assess the relative merits of paint-removal techniques within the time and funds allocated to this task in this program. It was agreed, however, that a controlled-environment chamber could be valuable for certain removal-method evaluations as well as for paint-application control studies. Thus, the majority of the paint-removal/worker-protection analyses were based on field operations, and a lesser number of analyses were based on chamber tests. Valuable information also was provided by the Iowa, Kentucky, Louisiana, North Carolina, and Wisconsin DOTs.

DISCUSSION

Paint- Removal Methods

There are many methods of paint removal, including abrasive or grit blasting, water jets, hand tools, power tools, chemical stripping, and heat. Each of these general methods consists of a number of subcategories as shown in TABLE 2.

An excellent comparison of many of the attributes of these methods is given in the Industrial Lead-Paint Removal Handbook by K. A. Trimber (see chapter 5, table 4). Additional comparisons based on our work in this program are provided later.

In the past, the most common paint-removal method has been abrasive or grit blasting. It is fast, and it removes paint, corrosion, and millscale to produce a clean surface with a good profile for recoating. Its main disadvantage is that it produces large volumes of dust. The dust contains very fine particulates from which the environment and the workers must be protected. The cost of this protection is high. Today, continuous blasting without containment will generate particulates in excess of the U.S. Environmental Protection (EPA) regulations. An alternative is vacuum blasting without confinement, but the removal rates are greatly reduced (approximately 80 percent). The added weight of the vacuum attachment tires the operator and the added bulk reduces mobility. In case of containment, building and moving the confinement structures are both costly and time consuming. In both cases, the used blast media and the paint debris need to be separated so the media can be recycled and the volume of hazardous waste can be reduced. This significantly reduces the cost of treatment and disposal of the waste.

Steel grit often is selected because it can be recycled repeatedly because of a low breakdown rate. It gives a good surface profile, and provides temporary stabilization against leaching of lead from the debris as measured by the toxicity characteristic leaching procedure (TCLP) test. Steel-grit blasting produces large numbers of paint debris particles with diameters of less than 1.0 µm. As discussed in greater detail later, size analysis of the particles collected on a filter within the blast confinement area showed that more than 50 percent of the particles had diameters less than 1.0 µm. Elemental analysis of these fine particles shows that they contain lead. It is difficult to determine how many particles with diameters less than 0.3 µm are produced by the blasting operation because such small particles pass through most filters and common particle size analysis techniques are not applicable below 0.3 µm. Particulates that contain lead/chromium and have diameters less than 0.3µm would present a hazard to the worker because: (1) they would not be totally removed by standard high efficiency particle absolute (HEPA) filters which are rated 99.97 percent efficient down to 0.3-µm size particles, (2) they would be difficult to contain within the confinement structure, and (3) they would produce contamination at greater distances from the work site.

Despite problems associated with grit blasting, its high removal rate outweighs the additional costs associated with worker and environmental protection when compared with other paint-removal options. In general, blasting within confinement is the method of choice when complete paint removal is specified, while vacuum blasting may be selected for spot preparation requirement. In this process, it is difficult to recover all dust and debris with the vacuum system. Very few additives are used in grit blasting. One exception is the addition of a material such as BlastoxTM which has been shown to help stabilize the lead in the paint debris against leaching in the TCLP test. A negative aspect of BlastoxTM is the need to keep it dry; when wet it clogs the blasting system.

Water jets can be used to remove the loose paint and rust, as well as salt, dirt, and soils. Advantages of this method are: (1) the degree of loose paint and rust removal can be altered by adjusting the water pressure, (2) the paint usually comes off in chips so that these chips can be collected on a porous tarp, while allowing the water to pass through, (3) the water temperature can be adjusted, and (4), it is relatively inexpensive. Disadvantages are: (1) the method, by itself, is not suitable for total paint, corrosion, and millscale removal; (2) it does not produce any surface profile; and (3) care must be taken to be sure all hazardous debris is contained and properly disposed. Paint removal by hand tools gives a minimally prepared surface. This may be satisfactory provided good surface-tolerant paints are available and limited coating lifetimes are acceptable. Handtool removal is probably the most operator sensitive of the removal methods. It has the advantage of producing the least debris and the debris that is produced can be easily collected on tarps.

Chemical stripping is used in certain cases, depending on bridge type and location. It is used most often to remove paint from tanks. This process involves messy, dangerous acidic or alkaline materials, often as gels, which are hazardous and require thorough rinsing and proper disposal.

Paint removal by laser was examined in the laboratory using a Coherent EFA51, 1500-W, continuous-wave CO2 laser. The substrates (test samples) were 102-mm (4-in) square or 51-mm by 102-mm (2-in by 4-in) rectangular sections of painted steel cut from bridge girders that had been taken out of service and stored by the Illinois Department of Transportation. The existing paint was a three-layer system consisting of a red-lead/alkyd primer, a leafing aluminum/phenolic matrix intermediate coating, and a green-pigmented, non-leafing aluminum/phenolic topcoat. The test samples were placed within a glass confinement system with a zinc selenide (ZnSe) window so that all byproducts from the removal process were contained. The containment system consisted of a 2-L glass filter flask with side tubulation and the bottom cut off. The test sample was placed on a steel-base plate to which the flask was sealed by vacuum-bagging tacky tape. The ZnSe window was sealed to the top of the flask and the side arm led through a TenaxTM adsorbent tube to a TedlarTM gas bag. The apparatus is shown in FIGURE 12.

The laser beam covered a 6.4-mm (1/4-in) diameter area of the sample surface. It was found that approximately 1 s of laser operation was sufficient to remove the paint without damage to the steel. Thus, the sample was moved to expose a different spot on the surface after each 1-s irradiation until sufficient byproduct could be collected for analysis.

Each time the laser beam impinged upon the painted surface, the paint burned with a yellow, sooty flame that rose 76 to 102 mm (3-4 in) above the painted surface. Visibility through the flask was reduced with each application of the laser. This was due to the fine soot that formed and was deposited on the sides of the flask. It scattered light within the flask and was deposited on the inner walls of the flask as shown in FIGURE 13. Larger, heavy soot particles fell to the bottom of the system, depositing on the base plate as well as on the painted sample itself.

Samples of the soot were collected from various parts of the apparatus and were analyzed by scanning electron microscopy (SEM) and energy dispersive x-ray (EDX). SEM micrographs of soot from the walls of the flask, from the base plate, and from the area where the byproduct gases escaped from the flask are shown in FIGURES 14, 15, and 16, respectively. By comparing the particle sizes with the 10-µm bar on the photos, it is evident that particles with diameters much less than 1 µm are prevalent. In fact, the larger particles appear to be agglomerates of finer particles.

The condition of the painted surface after being subjected to the laser beam for 1 s is shown in FIGURES 17a and 17b. Several different areas are apparent in the x 10 magnification photograph. The raised black area is where the charred paint has blistered up away from the steel. A portion of the char was broken off, revealing that there is still some residual red lead left on the steel as seen in the upper right-hand corner of the photograph. Some large pieces of soot deposited on untreated green paint are shown at the left and the bottom of the picture.

EDX analysis of soot samples shown in FIGURES 14, 15, and 16 demonstrated that the soot contains lead. The other elements detected by EDX were silicon and aluminum.

FIGURE 18 is a photograph of the surface after laser treatment. The photograph is at x 7 magnification and shading was produced by the light shining at an angle from the top of the photograph. Several interesting features are apparent. Over most of the treated area, the topcoats were removed leaving red-lead primer. Complete paint removal down to bare metal occurred only over a small area as seen near the top of the treated area. Residual aluminum can be seen along the periphery of the treated area.

The laser tests lead to the following conclusions:

  • Paint can be removed rapidly by laser treatment.
  • Care must be taken to insure complete paint removal.
  • Large volumes of soot are produced during paint removal using the laser.
  • The particle size of much of the soot produced by laser treatment is very fine (less than 1 µm).
  • The laser-produced soot contains lead and aluminum.

Since the use of heat or light sources to remove the paint would most likely result in similar conclusions to those above, they were not extensively studied.

IDOT PAINT-REMOVAL DEMONSTRATION - TESTING PROTOCOL

The Illinois Department of Transportation (IDOT) conducted a paint-removal demonstration program at I-55 between Wood and Damen Streets in Chicago, Illinois on April 22 and 23, 1993. The project was monitored in this study. The IDOT objective for the program was to familiarize contractors with various aspects of paint removal, including removal methods, Illinois DOT requirements, EPA and Occupational Safety and Health Administration (OSHA) requirements, full-containment structure construction, paint-condition determination, and analysis of paint/blast debris. The objectives of this study were to monitor the removal methods, assess and compare their advantages and disadvantages, obtain samples for TCLP and other analysis, and demonstrate thermal-wave imaging (task F) and electrochemical impedance spectroscopy (task E) as methods of evaluating existing conditions.

Work within this study was divided into three categories: tests before paint removal, tests during the removal processes, and tests after the paint removal. All of these tests, which are listed below, provided information directly related to the objectives of task B of this study. In addition, several of the tests, such as 1, 2, 3, and 4, provided information generally required in order to make an economic analysis to fulfill our task A objectives. Several of the tests (4, 5, 12, and 13) provide the type of data needed to address issues related to task C (Analysis and Disposal of Paint Debris), such as assessment of the degree of hazard and handling procedures for the waste debris. Paint debris samples were taken for TCLP analysis in order to verify results reported by others concerning the ability of steel blast media to stabilize the lead from leaching in the TCLP test. Other tests such as 2, 3, and 5, provided information relating to task D (Advanced Coatings).

Initial Tests

  1. Videotape the initial bridge steel surface condition.
  2. Measure the paint film thickness using dry film thickness gauge.
  3. Conduct paint adhesion tests using an Elcometer.
  4. Collect samples of existing paint for metals and chloride analysis.
  5. Measure lead (Pb) levels in existing paint using an x-ray fluorescence (XRF) paint analyzer.
  6. Collect water samples from web sections of girder to be washed.
  7. Document the initial paint surface condition of a section of bridge girder, similar to the one from which paint is to be removed, by thermal-wave imaging.

Tests Conducted During the Paint Removal

  1. Collect air samples as near as possible to the blast or tool surface during the paint-removal operations.
  2. Collect airborne particulates as near as possible to the blast or tool surface during paint-removal operations using filters and pumps.
  3. Measure temperature and humidity.

Tests Conducted After Paint Removal

  1. Measure lead (Pb) levels remaining on the cleaned surfaces using XRF.
  2. Collect samples of paint debris from each removal method and submit for total Pb analysis and toxicity characteristic leaching procedure (TCLP) testing.
  3. Laboratory tests:
    a. Analyze air samples taken during paint-removal operations using gas
    chromatography/mass spectrometry (GC/MS) for volatile organic compounds (VOC) determination.
    b. Analyze particulates collected on filters for metals content and size distribution.

Double containment was used in the demonstration in order to minimize the possible escape of dust from the grit-blast area. The containment structure was recorded on videotape for future reference and is part of the IDOT records but is not discussed further in this report. Details are available from IDOT. Entrance and exit from the containment area was via an anteroom or change room. The grit blasting was done using G-40 steel grit. The original paint film thickness was measured as 0.15-0.20 µm (6 to 8 mils). It was a three-layer system consisting of a red-lead/alkyd primer, a leafing aluminum/phenolic intermediate coating, and a gray non-leafing aluminum/phenolic topcoat. Adhesion varied significantly from area to area on this structure. Elcometer tests gave adhesion values of approximately 2067 kPa (300 lb/in2), but since the paint was brittle, it spalled off while crosshatching during the ASTM D3359-90 test (Measuring Adhesion by Tape Test, Method B - Cross-Cut Tape Test) producing a 0B rating (extremely poor adhesion). Weather conditions were mild throughout the 2-day removal demonstration. Temperatures ranged between 12.8 and 15.6°C (55°F and 60°F), and relative humidities were 35 to 45 percent. Details of the tests relating to task B are discussed below.

Analysis of Paint and Steel for Lead by X-Ray Fluorescence

Both the paint and the base steel were analyzed for lead content using a Princeton Gamma Tech (PGT) x-ray fluorescence (XRF) lead-paint analyzer. This work was done by George Cardis of Loyalty Environmental, Inc. of Skokie, Illinois. The XRF method gives results per unit area -- it analyzes approximately 1 cm2 of surface. For lead, it is accurate to ±0.5 mg/cm2. Paints with lead levels greater than 1 mg/cm2 are considered hazardous. Analysis of the base steel was needed to obtain a background lead level. The paint contained such large amounts of lead that all paint readings were off scale, i.e., greater than 10 mg Pb/cm2. After the various paint-removal methods were demonstrated, the cleaned-surface lead levels were again measured. It was found by visual inspection that grit blasting did drive a small amount of lead from the paint into the cleaned surface. This amount was below 0.5 mg/cm2 and thus was no longer considered as hazardous. Some concern has been expressed as to the possibility of the presence of sulfur resulting in false lead-concentration measurements by XRF. While it is true that the lead M series line measured at 2.3 keV is interfered by the sulfur K series line, the XRF device used during the IDOT test measured lead concentrations using the lead K series line at 74.9 keV with no interference by sulfur.

Although originally designed for use in homes, schools, and other buildings, the method is finding more and more use with steel structures. This is because the measurements are easy to make, they require only a few minutes to obtain, and the results are known immediately on site. If the owner does not want to purchase the equipment, consultants who will provide the service are readily available.

Water-Jet Cleaning Results

Water-jet cleaning of bridge girders was demonstrated under various conditions of water pressure and temperature. The chloride levels on the surfaces of the I-beams before and after water-jet cleaning were measured using two different sampling methods. In the first method, a plastic pipe elbow with an o-ring that could be sealed to the painted surface by hand pressure was used. The elbow was filled with 60 mL of deionized water which was allowed to remain in contact with approximately 15 cm2 of the surface for 30 s and then was poured into a plastic container by rotating the fixture. This method was used to sample the surface of the vertical portions (webs) of the I-beams before and after water-jet cleaning.

In the second method, runoff water from the water-jet cleaning operation was collected at the start of cleaning and at the end of the cleaning. The initial sample contained both soluble and insoluble contaminants including loose rust, loose paint, dirt, and salts coming from the horizontal flange areas as well as from the vertical web area. The final sample contained only soluble materials. The pH of the initial water runoff sample taken under conditions of 17914 kfa (2600 lb/in2psi water pressure and a starting water temperature of 99.9°C (210°F) was 5.0 while that of the final run-off sample at the end of the cleaning was 5.5. The water-sample analyses are given in TABLE 3.

The chloride content of the starting water was subtracted from each sample analysis and the results were reported in TABLE 3 as milligrams of chloride per square foot of girder surface. The results indicate that the plastic-elbow device gives reasonably reproducible results since the two samples taken before cleaning (1A and 1B) had essentially the same chloride content as did the two samples (2A and 2B) taken after cleaning. Since these samples were[B taken from a vertical portion of the beam, there was little or no accumulation of salt and dirt on the area sampled. Although the chloride levels were rather low to start with, washing gave approximately a 70 percent reduction in chloride.

The water-jet runoff samples contained much more chloride, probably due to an accumulation of salt on the I-beam flanges. The chloride level in the initial sample was 12953 mg/m2 (1205 mg/ft2). Washing gave a 94 percent reduction in chloride down to a final level of 120 mg/m2 (11.2 mg/ft2). The initial sample also was slightly more acidic than the final sample. In other water-jet cleaning trials conducted in this program and by IDOT, the use of unheated water gave results very similar to those obtained with hot water. As a result, IDOT has standardized on cleaning with unheated water.

Air-Sampling Tests for VOCs Generated During Grit Blasting Within Confinement

No volatile organic compounds (VOCs) were found in a vacuum-bottle test of the atmosphere in the confinement area during grit blasting. In addition, no VOCs were collected on a TenaxTM adsorbent tube through which the confinement area atmosphere was continuously cycled during the blasting operation. This is the expected result since there were no organic solvents involved and no heat to cause thermal decomposition of the paint.

Three different air-sampling tests were conducted within the confinement area during the steel-grit blasting procedure. The first test was a vacuum-bottle test in which the valve on an evacuated sampling bottle was opened within the confinement area during blasting to collect an air sample. The objective was to determine whether or not the process produces any significant quantity of VOCs. Analysis of this sample by gas chromatography/mass spectroscopy (GCMS) did not indicate the presence of any VOCs resulting from the blasting.

The second test also was a test to determine whether or not VOCs are produced during the blasting process. In this test, a small pump was used to continuously draw air through an adsorbent (TenaxTM) tube at 20 cm3/min. Organic contaminants in the airstream are adsorbed and later in the laboratory are driven from the adsorbent into a GCMS for analysis. This test is better suited to the determination of small concentrations of VOCs than is the vacuum- bottle test since a much larger volume of air is used in this test and the VOCs are concentrated by adsorption. Nevertheless, no VOCs were detected.

Airborne Grit-Blast Debris Particulate Sampling and Analysis

The objective of this air-sampling test was to determine the size distribution and composition of particulates in the air within the confinement area during and after blasting. Samples were collected by drawing ambient air through an 0.8-µm mixed cellulose ester (MCE) in-line filter at a rate of 400 cm3/min for a total period of 90 min of which only the first 10 min was actual blasting time. The remaining 80 min was time during which blast debris was being vacuumed out of the confinement area. From the weight of the collected residue and the flow of 400 cm3/min over the full 90-min period, an average airborne particulate concentration of 280 mg/m3 is calculated. The residue was analyzed for particle-size distribution by the Coulter technique and by an ElzoneTM particle-size analyzer. Particulate size, shape, and composition were determined by scanning electron microscopy (SEM) and energy-dispersive x-ray (EDX) microanalysis. Particle-size analysis results indicate the presence of many particles having diameters less than the nominal 0.8-µm filter porosity are present in the filter cake. This apparently is the result of partial clogging of the filter porosity as the residue built up during the test. The filter cake was thicker in the center of the in-line filter due to the high airflow rate.

Coulter particle size analysis: Filter-cake particulates were dispersed in a saline solution using an anionic surfactant to prevent the particles from agglomerating. The Coulter Counter particle-sizing system allows for a measurement of a size distribution between certain minimum and maximum particle size diameters depending of the orifice sizes chosen. A range of 2 to 60 µm was chosen for analysis because preliminary SEM analysis indicated that the smaller particles tended to be more rich in lead. FIGURES 19a and 19b depict the particle-size distribution obtained for two samples taken from different areas on a single filter cake. Sample #1 was taken from an area near the outer edge of the filter while sample #2 was taken from an area near the center of the filter. The plots in FIGURES 19a and 19b are most easily understood by imagining the particles passing through a series of sieves with mesh sizes indicated on the horizontal axis. The height of each vertical line (or bar) represents the number of particles of that size. Neither sample contained many particles with diameters greater than 10 µm. The plot in FIGURE 19a indicates that 50 percent of the particles are smaller than 2.5 µm in size. The plot in FIGURE 19b indicates that of all the particles measured in the 2 µm to 60 µm range, the largest number occurred at the 2-µm cutoff. Since this strongly suggests that a large portion of the particulates have diameters less than 2-µm, samples were sent out for analysis by the ElzoneTM system, which was capable of measuring sizes down to well below 1 µm. These samples were representative of the remainder of the filter cake after having removed the two small samples analyzed in FIGURES 19a and 19b.

ElzoneTM particle size analysis: The ElzoneTM technique is similar to the Coulter technique. The difference was that in the ElzoneTM case, a smaller orifice (capable of detecting particle diameters down to 0.6 µm) was used. Two samples were analyzed and the results are shown as number percentages in FIGURES 20 and 21 and volume percents in FIGURES 22 and 23. For the sample corresponding to FIGURE 20, more than 50 percent of the particles detected had diameters less than 0.8 µm and the highest number count occurred at 0.65 µm. For the sample shown in FIGURE 21, more than 50 percent of the particles had diameters less than 1.0 µm and the highest number counts occurred between 0.65 µm and 0.73 µm. Although neither sample contained a large number of particles with diameters greater than 6 µm, the larger particles make up a significant volume of the total particulate volume as shown in FIGURES 22 and 23. Note that the sample in FIGURE 22 contained a 10-µm latex marker.

The increased residence time of the smaller particles aerosol degrades visibility and air quality within the containment zone and raises safety concerns as the particle size approaches the filtering efficiency of different classes of respirators. Neither the Coulter CounterTM nor the ElzoneTM system were capable of determining whether or not particles with diameters less than 0.3 µm (the porosity of HEPA filters) were present.

SEM and EDX microanalysis: The air filter was heavily loaded with particulates. Sample particles were prepared for analysis in the SEM using two different techniques. The first technique entailed scooping particulates from the filter and dispersing them in semiconductor-grade acetone. The suspension was then transferred via pipette to a spectroscopically pure carbon plate. The second technique relied on electrically conductive adhesive carbon tape that was gently pressed against the surface of the filter and then mounted on a carbon plate. Both techniques produced satisfactory dispersions as indicated in FIGURES 24a and 24b that show the acetone dispersion at x 200 and x 500 magnifications and FIGURES 25a and 25b that show the carbon tape dispersion at x 200 and x 250. The SEM photomicrographs indicate that a wide variation is particle size is present in the airborne grit-blast debris.

FIGURES 26a and 26b show the top surface of the filter cake together with its energy-dispersive x-ray spectrum (EDX) and composition. The primary constituents are lead and calcium from the paint, iron from the steel grit and rust, and minor amounts of aluminum and magnesium that may come from the paint or from residual dust. The detection of silicon separately and in combination with aluminum is nearly always due to ambient dust. Note that this x-ray spectrum and the spectra that follow were acquired with an x-ray detector that uses a beryllium window to insulate the x-ray detecting crystal from the vacuum in the SEM. Although the beryllium window ensures proper operation of the detecting crystal, it completely absorbs low-energy x-rays from elements lighter than sodium. Therefore, elements such as oxygen, nitrogen, carbon, and hydrogen are not detectable. Three large fragments of steel grit found in the filter cartridge are shown in FIGURES 27a and 27b. Note that no lead was detected on the steel grit within the detection limits of the system. Smaller iron-containing particles were also detected, typically in the size range down to approximately 10 µm. Two such particles are shown in FIGURES 28a, 28b, 29a, and 29b. The iron-rich particle shown in FIGURES 29a and 29b also contains lead and silicon. These two particles may contain significant amounts of rust since they are morphologically different compared with the steel grit in FIGURES 27a and 27b.

The majority of particles analyzed contained lead, although some did not. Representative samples of particles are shown in FIGURES 30a, 30b, 31a, 31b, 32a, 32b, 33a, 33b, 34a, 34b, 35a, and 35b. The particle in FIGURES 34a and 34b contains significant amounts of lead and silicon together with iron, magnesium, calcium, and zinc. It may have come from the topcoat that had dust blown on it before it had cured. FIGURES 35a and 35b show a particle that is primarily zinc and probably originated from an intermediate layer of paint between the primer and the topcoat.

The proportion of particles that contain lead as a major constituent appeared to increase with decreasing size. Smaller particles, down to approximately 1 µm, are shown in FIGURES 36a, 36b, 37a,37b, 38a, 38b, 39a, and 39b. The angular morphology, together with the cleavage step appearance of these smaller particles, suggest they originate from a brittle layer, possibly the primer that is fractured by impingement of steel grit. TABLE 4 gives the composition of various sizes of particles collected on the filter within the grit-blast confinement area. The figure number of the corresponding SEM and EDX analyses also is listed in TABLE 4.

Effectiveness of Paint-Removal Procedures

Three types of paint-removal methods were compared in the demonstration. They were vacuum steel-grit blasting, steel grit blasting in full containment, and vacuum power-tool cleaning. All blasting was done using G-40 steel grit. Two vacuum power-tool system suppliers demonstrated the use of their equipment. Needle guns, roto-peening, and abrasive-disc cleaning tools were demonstrated by both companies. The debris collected for analysis from each power-tool company's cleaning work was a combination of debris from all three types of tools.

A qualitative comparison of these methods is presented in TABLE 5. It is based solely on observations made during the demonstration. Each method has advantages and disadvantages and the method of choice depends on the size, location, and geometry of the bridge being refurbished, as well as the size of area to be coated, degree of surface preparation required, etc.

JULIEN DUBUQUE BRIDGE AT DUBUQUE, IOWA

Paint debris samples were obtained from a paint-removal and recoating project on the Julien Dubuque Bridge over the Mississippi River between Dubuque, Iowa, and East Dubuque, Illinois, done by the Iowa Department of Transportation. The paint-removal method used was steel-grit blasting with full containment. This required bringing a preconstructed scaffolding under the bridge on a barge, raising the scaffolding up under the bridge as shown in FIGURES 40a and 40b, and putting the confinement structure in place. The grit-recovery system consisted of vibratory grit separation, air washing, and cyclone separation, but did not include a magnetic separation step.

This bridge was originally painted in 1942 using a lead pigment. In 1976, the paint was removed from all the easily accessible areas by grit blasting and the bridge was recoated using a zinc chromate pigment. Paint was removed from the areas not blasted in 1976 using vacuum-blast equipment. This paint debris is a combination of the original lead-based paint and the 1976 zinc chromate system.

The following debris samples were collected: (1) Wheelabrator GL40 steel grit, (2) used GL40 grit prior to cleaning, (3) paint waste separated from the used grit by the separation/recycling system, (4) debris obtained by magnetic separation from steel grit initially treated by the separation/recycling system, and (5), a sample of the vacuum blast debris described above. No analysis was done on the first two samples. The other three samples were examined by SEM as shown in FIGURES 41a, 41b, and 41c and by optical microscopy as shown in FIGURES 42a, 42b and 42c. They also were analyzed by EDX and these results are shown in FIGURES 43a, 43b, and 43c.

The material magnetically separated from the once-treated grit (see FIGURE 43a) is very high in silicon and, in fact, appears to contain glass or sand particles. The other main component identified is iron which came either from the steel blast media or from the structure itself. The sample was extremely nonuniform in composition and contained some fibrous materials (perhaps wood). It appeared to contain only small amounts of actual paint components such as red lead and zinc chromate. In fact, several other elements such as aluminum, magnesium, calcium, and titanium, were found in similar small concentrations. Sieve analysis of this sample showed that despite its very dusty brown appearance, less than 6 percent of the sample by weight was smaller than 45 µm in diameter (passed through a 325-mesh screen sieve).

The paint waste sample (FIGURE 43b) is very high in iron. This sample also contains silicon, although at a much reduced level compared to the magnetically separated sample described above. Lead, zinc, and chromium as well as magnesium, aluminum, calcium, and titanium were also found. The relatively low levels of lead in the paint waste are consistent with the fact that most of the lead had been previously removed. This sample contained the largest amount of fines. More than 20 percent of the sample passed through a 45 µm screen.

The vacuum blast debris sample (FIGURE 43c) contains many elements including lead, chromium, iron, and zinc, that are present in relatively large amounts. This analysis is consistent with the paint records that show that both red-lead and zinc chromate pigments were used in the paints. Again, the iron most likely comes from steel or rust. This is the only paint-waste sample from the Dubuque site that actually looks like it contains paint. Some of these paint particles clearly show four layers of paint under optical microscopic examination. Approximately 16 percent of this sample was finer than 325 mesh (45 µ m).

The fines (the portions that passed through the 325-mesh sieve screen) from each of the above three samples were also examined by SEM. FIGURES 44a, 44b, and 44c show the <45-µm particles in the magnetically separated material at magnifications of x 500, x 5,000, and x 50,000. In the x 500 photomicrograph, particles ranging in size from less than 1 µm up to about 30 µm are clearly discernable. The x 5,000 photo shows a less than 0.5-µm particle nest to an approximately 10-µm-diameter particle. The x 50,000 photo shows only the 0.4-µm-wide particle.

FIGURES 45a, 45b, and 45c show a similar set of photomicrographs for the paint-waste particles that passed through the 325-mesh screen. FIGURES 46a, 46b, and 46c present the results for the vacuum blast fines. In each of the three sets of figures, the particle featured at x 50,000 can be identified in the x 5,000 and x 500 photos upon close examination. Particles smaller than 0.3 µm in diameter appear to exist in each of the samples, but since this size is near the limit of resolution of the instrument, further study is needed to establish whether or not such small particles are present, and if so, how many.

Two particles, approximately 0.5 µm in diameter, from each of the above three samples were analyzed by EDX. The results are presented in FIGURES 47a, 47b, 48a, 48b, 49a, and 49b. For the paint-waste samples separated from the grit by air and magnetically, one particle contained lead and the other did not. For the vacuum blast debris, both particles contained lead. Again, these results demonstrated that the fine particles produced during grit-blasting operations contained lead.

 

Home | About | Research | Technology Transfer | Education | Managament & Policy | Information Resources | Contact

Last updated: July 12, 2006    © 2005 Infrastructure Technology Institute