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Fire Research Division

NIST Combinatorial Methods Center Focused Project


Statement of Work Focused Project 
Agreement
NIST Combinatorial Methods Center
 Web Site


High Throughput Flammability Test Methods for Compositionally Graded Samples

We are very excited about the potential this program has to impact the speed of R&D in the flame retardants and polymer additive areas.

The Fire Research Division at NIST has allocated over $650K of internal funding for 2002 for High Throughput flammability research. Membership in this Focused Project on High Throughput Flammability Test Methods affords members an excellent opportunity to leverage their R&D funds for the purpose of gaining information, knowledge and skills in the high throughput field. This is also an opportunity for the members to help set the direction for the development of these new R&D tools.

STATEMENT OF WORK

Project Leader: Jeffrey W. Gilman
Phone: 301-975-6573
Email: jeffrey.gilman@nist.gov

Introduction:

Flammability performance standards for new materials are most often met through the use of additives. To ensure compliance, complex mixtures containing the polymer resin, stabilizers, processing agents, pigments, and flame retardant additives are formulated, characterized, and tested one at a time. While it is in the interests of the public that flammability testing continues to be a critical component of materials research and development (R&D), there are no guarantees that innovation cycle times can be sufficiently reduced using this approach to respond to the competitive pressures of the global marketplace. The recognition that industry needs more efficient tools for materials R&D has prompted the Building and Fire Research Laboratory (BFRL) at the National Institute of Standards and Technology (NIST) to initiate a program of research directed at the development of high-throughput (or combinatorial) methods for materials flammability research. In this context, we use the term "high-throughput" to refer to a research strategy characterized by conducting many experiments at the same time. By virtue of its inherent efficiency, this approach will provide us with the capability to explore compositional space and thereby develop a better understanding of the interactions between components and their effects on the ultimate performance of these materials. This knowledge can be used by industry to determine optimal compositions with respect to materials flammability and other properties of interest.

Technical Approach:

A high-throughput method for evaluating the flammability performance of experimental formulations under realistic processing conditions is needed to complement the work we are doing in developing micro-scale platforms for lead discovery motivated R&D. Our approach is embodied in the device, known as the continuous gradient extruder (CGE), depicted in the Figure 1. The CGE consists of a series of programmable gravimetric feeders capable of producing a constant compositional gradient in an extruded polymer strip and sensors that monitor both the concentrations (by quantitative infrared spectroscopy) and degree of dispersion of the additives (by changes in the dielectric response). In principle, each sample contains a wealth of information about the effects of composition on the flammability of the base polymer. This obvious extension of existing technology will enable researchers to screen hundreds of possibilities, as determined by variations in the relative amounts of critical additives, in the same time it now takes to test just a couple of formulations.

 

 

Prototype extruder

Figure 1. Prototype extruder capable of producing polymer samples with multiple additives having concentrations that vary linearly along the length of the strip.

Preliminary Results:

A compositionally graded sample containing ammonium polyphosphate (APP) and pentaerythritol (PER) in polystyrene was produced in the CGE and burned in our horizontal ignition flammability test (HIFT) device under a constant flux of (16.8 ± 0.4) kW/m2. The sample was a strip (approximately 1.5 m long, 7 mm wide and 2 mm thick) consisting of PS blended with varying amounts of a 3:1 mixture of APP and PER. We choose the upper limit of concentration at 30 % since this formulation has a V-0 rating in the UL94 V test. We attempted to create a linear concentration gradient (from C = 0 % to C = 30 % additive by mass) by increasing the rate of feed from the hopper containing the mixture of APP and PER linearly with time.

Apparatus for measuring flame spread over gradient samples.

Figure 3. Apparatus for measuring flame spread over gradient samples.

 

The flame velocities were measured by pulling the extruded strip through a 300 mm heating zone (Fig 3.) such that the flame front remained at a fixed position. The results are plotted in Figure 4. The data (t) was collected at 50 mm intervals, which were marked off on the strip, with the initial point (at x = 0) corresponding to the pure polymer (C = 0 % at x = 0). The solid line was obtained by fitting the experimental data to a hypothetical function (exponential) that was derived by assuming a linear dependence between flame velocity and additive concentration, which was also assumed to decrease linearly with distance. The validity of these assumptions is supported by the fact that this function does a good job of representing the experimental data. The derivative of the function in Figure 4 is a linear function of x (or C = ax) with a negative slope (a) (e.g. Fig 6) indicating a reduction in the flame velocity with increasing concentration of additive as expected.

 

The progression of the flame front as a function of time measured for the PS/APP/PER gradient.

Figure 4. The progression of the flame front as a function of time measured for the PS/APP/PER gradient. The solid line was obtained by fitting the experimental data (circles) to a hypothetical function derived on the basis of assumptions stated in the text.

 

 

The progression of the flame front as a function of time measured for PS/clay gradient.

Figure 5. The progression of the flame front as a function of time measured for PS/clay gradient. The solid line was obtained by fitting the experimental data (circles) to a hypothetical function derived on the basis of assumptions stated in the text.

 

Plot of flame speed versus composition.

Figure 6. Plot of flame speed versus composition.

 

Comparable data was collected for a PS/clay gradient sample with an approximately linear concentration gradient of clay varying from 0 % to about 10 % by mass. In this case, the flame velocities were observed to accelerate with increasing clay concentration (Figure 5), suggesting that the presence of the clay actually enhances the spread of flames over the surface of this material. This observation is consistent with our previous observation that polymer/clay nanocomposites ignite at lower temperatures (even though, once ignited, they tend to burn with a lower HRR) than the pure polymer, since lower ignition temperatures facilitate flame spread. Eventually, we would like to make simultaneous measurements of both flame velocity and heat release rate (HRR) to determine the optimal composition, which results in the best compromise between flame spread and HRR.

This approach will also allow us to evaluate the large variety of combinations and parameters associated with the flame retarded polymers.

Project Deliverables:

The project team will assemble, calibrate and demonstrate a prototype High Throughput Flammability screening system for making simultaneous measurements of the HRR and flame spread velocities of compositionally graded samples as a function of the incident flux. This prototype system will initially consist of the apparatus described above. A test method will be developed and validated by correlating the results with conventional measurements, such as cone calorimetry and UL-94, or with other fire tests, which the members desire studied. This High Throughput sample preparation, characterization and flammability screening will be complimented with High Throughput physical property characterization (modulus and elastomeric properties) of the gradient samples (before burning and after) using an automated Nanoindentor.  An Annual Report will be delivered to the members within 2 months of the end of the project.

Project Meetings and Web-site:

We will have 3 meetings during the Project. One at the 1 month point, for the purpose of finalizing the research plans, and the second and third meetings will occur at 6 and 11 months after the start of the project, respectively. The purpose of these later two meeting is to share results and plan future experiments with Project members. A web-site will be available to members to facilitate communication of Project results and administrative information.

Project Milestones:

These milestone will be completed by the end of the first full year of the Project. Membership is for one year at a time, therefore we have only included plans for year one in this document. Plans for a second year will be discussed at the third Project meeting.

Membership Fee:

The membership fee is $20,000 per year.

Upon execution of the attached Project Agreement the fee and agreement should be sent to:

NIST
Attention Sharon Rinehart
100 Bureau Drive
Gaithersburg, MD USA
Mail Stop 8602
sharon.reinhart@nist.gov
301-975-5876

 


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Date created: 3/5/2002
Last updated: 3/5/2002