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SEMI® F57-0301 and beyond:
Advancing standards for ultra high-purity fluoropolymer components


James M. Hanson, Swagelok Company; Ronnie A. Browne & Robert A. Shutler, Swagelok Semiconductor Services Company, Santa Clara, California, USA

Overview
New wet processes for semiconductor manufacturing, employing slurries, as well as HCl and HF at higher pressures and temperatures, are requiring higher standards for purity and improved design and materials for fluid-system components. OEMs, toolmakers and integrators are calling for longer life cycles, easier maintenance, resistance to permeation and reduced particle shedding in valves and other system components.

SEMI F57-0301 provides baseline standards for purity, which are attainable assuming proper material selection, methods of design, manufacturing and quality-control testing. Third-party test results presented in this article corroborate this point of view. However, if SEMI F57 is to remain current, it must incorporate additional testing methods and even more stringent testing standards that have been developed by leading OEMs and circulated within the industry. Such testing includes BOC Edwards

Dycon ExSM dynamic extraction test, which utilizes 37 per cent HCl, as well as other reliability tests with slurries, HCl and HF. Methodologies and conclusions discussed in this article are applicable not only to valves but also to many other liquid system components, such as flow meters, filter housings and regulators.

The drive toward higher standards
Increased use of liquid processing, together with new processes and materials, such as abrasive slurries for chemical mechanical planarization (CMP), are necessarily driving the requirements for improved performance and reliability in fluid-system components. As the industry moves toward larger wafer sizes, and narrower and denser line widths, greater demands are placed on the purity of fluid-system components. Productivity, profitability and process yield are directly related to overall system component performance. Such trends led to the development and approval of SEMI Standard F57-0301 on October 18, 2000.

The purpose of the standard is to specify the minimum performance requirements for ultrahigh-purity (UHP) polymer components used throughout semiconductor ultrapure water and chemical distribution systems. The scope of the standard encompasses polymer component purity and mechanical specifications, along with references for qualification test methods. Certification, traceability, and packaging requirements are also included. However, the standard focuses primarily on purity requirements, leaving mechanical requirements such as dimensional tolerances, flow characteristics, leak integrity, and mechanical strength to the supplier’s discretion.

This article will discuss and provide evidence in support of SEMI F57, and in support of more stringent industry standards that should be incorporated into the SEMI standard. It will also provide some guidelines concerning the design, material selection and manufacturing of fluid-system components that enable component suppliers to meet the industry’s most stringent standards.

Overriding design criteria
In developing components for ultrahigh-purity applications, the fluid-system designer must be in close touch with the present and future requirements of leading OEMs, toolmakers, and integrators. Communication must be ongoing and thorough. The following points concerning next-generation valve design reflect communications with leading equipment manufacturers.

    1. Design should exceed, where possible and practical, the current purity requirements of SEMI F57.
    2. Design efforts should focus on the most challenging process requirements, such as those involvingCMP and acids. Next-generation valves should demonstrate superior performance in any liquid chemical distribution system.
    3. Designs should address long life, reliability, and ease of maintenance. These issues should be given equal weight, as compared to initial performance issues, such as pressure/temperature ratings and footprint.
    4. Designs should be statistically and data driven, given the availability of thresholds required by the industry.

       


      Material selection and manufacturing
      Given the above design criteria, particularly references #s above, material selection is critical. Traditionally, suppliers of highpurity valves for the semiconductor industry have chosen perfluoroalkoxy (PFA) for wetted components. PFA is produced by the copolymerization of TFE and perfluoroalkyl monomers. These are produced by reacting fluoroepoxide with a metal fluoride to obtain an acid fluoride, which is then pyrolyzed over calcium carbonate to obtain propylvinyl ether (PVE). In recent years, Dupont, Dyneon, and other fluoropolymer resin manufacturers have been improving the purity of PFA.

      However, in certain fluid components, such as valves, there is good reason to call PFA into question, given the ever increasing demands for higher-purity wetted surfaces, as evidenced in SEMI F57 and in higher performance requirements for acid and CMP processes. The alternative to PFA is PTFE, which is inherently less reactive than PFA and has superior chemical resistance and qualities for purity. It may well be the material of choice for next-generation wetted components.

      PTFE, the original fluoropolymer resin, is simply polymerized TFE. It has a less complex structure than PFA and requires less processing to reach a usable state. Dupont’s Teflon® NXT grade of PTFE (modified PTFE) provides the following superior benefits: high purity, ease of machining, and resistance to acids, abrasives and other operating stresses. It contains less than 0.01 per cent PPVE, so it is still considered PTFE.

      Historically, most high-purity valves have been manufactured using injection molding manufacturing technology, but this technology carries with it certain risks from a purity standpoint. PFA, the material of choice for injection molding, must pass through several processes in close contact with metal (Figure 1). Melt extrusion of PFA into molding pellets occurs in an extruder with a metal barrel and screw that conveys the highly corrosive PFA melt at temperatures in excess of 300°C through a metal pelletizing die. These PFA molding pellets are then remelted at temperatures in excess of 300°C in the injection molding process. Again, the molten PFA is conveyed in a metal barrel and screw and then into a high-temperature metal injection mold die to form the final valve shape.

      By contrast, the manufacturing of wetted components with PTFE is a cleaner process that helps to eliminate metallic contamination. Sintering of PTFE is accomplished in block form. Machining of the block into a valve occurs without lubricants, using special cutting tools at room temperature. Further, precision machining is performed at closer tolerances, as compared to injection molding. In addition, machining enables faster and more economical development and turnaround time for product development and manufacturing process development. It allows for great flexibility in changeovers between valve configurations.



      Design and flow path
      Table 1 translates desirable valve attributes into design guidelines. The attributes are based on SEMI F57 and other industry requirements, whereas the design guidelines are based on the principles of physics and valve geometry. In large part, Table 1 underscores the following axiom: The valve must not adversely affect critical fluids (such as slurries), and the critical fluids must not adversely affect the valve. Six of the eight guidelines in Table 1 are in part, if not wholly, related to flow path within the valve. Flow path is a critical consideration, not only from the standpoint of SEMI F57 purity requirements for particle contribution but also from the standpoint of recent advances in semiconductor manufacturing, such as copper CMP, which requires gentle treatment of slurries to minimize agglomeration.

      Cross section of a fluoropolymer UHP shut-off valve

      Figure 2. Cross section of a fluoropolymer UHP shut-off valve, with labeled sections and parts. The PTFE body incorporates a large bowl or cavity for gentle treatment of sensitive medium like copper CMP slurries.

      Many valves employed in the semiconductor industry today were not designed for today’s advanced processes. In fact, their design sometimes predates the invention and widespread use of these processes. Computational fluid dynamics (CFD), the leading computer-aided modeling tool for fluid systems, enables engineers to model different geometries (with different critical system fluids) to determine how those geometries will perform and whether they meet the design guidelines in Table 1. CFD predicts the flow coefficient for any given valve design. It also illustrates and calculates fluid velocity; shear forces and incremental pressure drops throughout the valve. In terms of fluid flow, the body and diaphragm are the most important sections of the valve (Figure 2). CFD enables the designer to hold certain design elements constant while experimenting with others for optimized performance of the flow path.

      For example, a designer may experiment with the size of the inlet and outlet orifices or their angle in relation to one another. Or, he or she may focus on the shape of the bowl or cavity itself, in combination with the diaphragm geometry. Besides flow path, Table 1 addresses issues of material integrity and wear, particle shedding and permeation, all of which may be tested at the design stagethrough finite element analysis (FEA).

      FEA provides the fluid component engineer with a time-stepped analysis of the stresses and deformation of each material or component section, such as the diaphragm and seat seal. FEA is particularly valuable in the design of extended life cycle fluoropolymer diaphragms, which must resist permeation and attack by acids, slurries and other critical chemicals used in the semiconductor industry. While extended life cycle requires a flexible diaphragm, resistance to acids requires a thick diaphragm. FEA assists the engineer in determining the best balance between these two competing requirements.

      In employing FEA software, designers designate material properties; boundary conditions, such as temperature and pressure; stress limitations; and diaphragm geometry. The program then models and tests designs in three-dimensional space. Results enable engineers to experiment with diaphragm contours, thickness and functionality until the desired or optimal design is reached.

      High-purity testing
      As noted earlier, SEMI F57 focuses on purity, particularly static leach tests utilizing DI water. The standard is specific in identifying levels of ionic metallic and total organic carbon contamination that could lead to complications in semiconductor manufacturing. Given the increasing demands of OEMs, integrators and toolmakers, SEMI F57 performance levels should be regarded as baseline or minimum requirements.

      Unfortunately, there are some in the industry who question whether SEMI F57 is realistic, attainable, or too exacting. The SEMI standard is, first and foremost, a means of communicating between those who use and those who make fluid-system components. If OEMs or toolmakers desire a particular standard, fluid-system manufactures must determine if, in fact, the standard is attainable and repeatable under independent testing conditions. Tables 2–4 contain results for surface extractable contamination tests performed on the Swagelok® DRP™ Series UHP Fluoropolymer Diaphragm Valve. The independent tests were conducted by CT Associates, Inc., in accord with SEMI Standard F40 testing procedures. SEMI F57 contamination limits are provided in the tables for reference and comparison.







      While static leach tests required by SEMI F57 provide solid baseline performance guidelines, most field applications are dynamic, not static. Dynamic leach tests, not only for DI water but also for HCl and HF, as required by leading OEMs in the semiconductor industry, should find their place in the SEMI standard.

      One such test is BOC Edwards’ Dycon ExSM dynamic extraction test, which utilizes 37 per cent HCl. HCl is an appropriate medium for aggressive testing because it is one of the most effective chemicals in permeating fluoropolymers and in extracting metallic particles. Dycon ExSM employs minimal chemical volume over time, enabling detection of extractables at very low levels. The industry expectation is <20 ng/cm2 for bulk chemical extraction for the area normalized surface contamination from 37 elements extracted. The requirement for the area normalized extraction rate is <0.5 ng/cm2/day at 7 days. With proper component design and manufacturing procedures, these standards are attainable.





      CT Associates conducted the Dycon ExSM dynamic extraction test with the DRP series valve and results were well under industry limits (Table 5). The area normalized surface contamination from 37 elements extracted was 9.36 ng/cm2. The area normalized extraction rate was 0.06 ng/cm2/day at 7 days.

      Besides tests for ionic, metallic and total organic carbon contamination, SEMI F57 requires a test for particle contribution. This test calls for a rinse-timed test with DI water, followed by cycle evaluations. The objective is to measure particle shedding resulting from valve actuation, as well as subsequent cleanup over time. This is an important test, but unfortunately, specific limits for particle contribution have not been designated in the standard because no consensus has been reached.

      While some individuals (or companies) doubt that particle contribution can be measured reliably with repeatable results, there is growing acknowledgment that it can. Leading OEMs have issued standards pertaining to particle shedding. Table 6 represents particle contribution test results for the DRP, performed by Air Liquide-Balazs™ Analytical Services and corroborated by CT Associates.

      In field applications, semiconductor components process acidic chemicals, which, in some cases, may undermine component integrity and increase susceptibility to particle shedding. Future iterations of SEMI F57 should look toward additional media, such as HCl and HF. Testing protocols for acids, slurries and other critical chemicals should be an integral part of any UHP fluoropolymer valve design, manufacturing, and testing process.


      SEMI F57 should also look toward longer, more rigorous testing for particle shedding. While life-cycle testing is not the focus of SEMI F57, it is germane to issues of purity and particle shedding. How does extensive life-cycle testing in HF or HCl affect a valve’s particle shedding? How many liters of DI water are required to flush the valve clean after testing in HF or HCl? What is the overall projected cost of ownership given the amount of DI water required to bring the particle count down to acceptable levels?

      One standard issued by a major equipment manufacturer requires accelerated life-cycle testing in fluids appropriate to the valve’s intended use, such as HCl or HF. Accelerated life-cycle testing evaluates the statistical number of cycles, designated as the B10 life, where 10 per cent of the valves would be expected to fail. In accord with the industry standard, CT Associates tested the 1⁄2-inch DRP in 49 per cent HF, checking the test valves for cracking pressure and port-to-port pressure every 150,000 cycles. Since the valves were not cycled to failure, the Weibayes method (R. B. Abernethy, The New Weibull Handbook, 2000) was used to calculate the B10 life. Table 7 documents the calculated outcomes, as well as the industry standard.







      The same industry standard identifies specifications for particle shedding tests. First, a passive flush test measures the amount of DI water required to bring the particle contribution down to <0.1 particles/ml, with a designated particle size of < 0.10 μm. The standard calls for <300 ml. Second, a cycle test records the number of on-and-off cycles required for the valves to produce less than 100 particles per actuation, with a designated particle size of < 0.10 μm. Tables 8 and 9 contain test results for the 1⁄2-inch DRP before and after HF life-cycle testing, with reference to the industry standard. The tests were conducted by CT Associates.

      Conclusion
      SEMI F57 is an attainable, appropriate and useful standard for measuring the purity of fluoropolymer components. With appropriate selection of materials (modified PTFE for all wetted surfaces), advanced manufacturing practices (machining), utilization of computer-aided modeling techniques, and rigorous third-party testing, it is possible to design and manufacture components that meet or exceed this SEMI standard.

      However, if SEMI F57 is to remain a viable and relevant standard, additional tests and standards already in use within the industry must be incorporated. These new standards, while stringent, are attainable and appropriate, given current processes and practices in the field. They include dynamic leach tests, life-cycle and particle-contribution testing, and tests utilizing specific mediums used in the semiconductor manufacturing process, including slurries, HF and HCl.



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