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The High-bandwidth Digital Data Network:
A New Tool for Process Improvement

Including A Sampling of Digital Mass Flow Data To Illustrate The Benefits
By Jon Goldman


Recently JGA, in cooperation with Brooks Instrument, explored developing a software package to give end-users access to the bells and whistles that digital mass flow products provide. This project opened my eyes to the potential this technology offers for routine monitoring of many different types of critical sensing components in addition to MFCs. In this article I present some sample data extracted from a simulated Single-Wafer CVD System equipped with a bank of digital MFC prototypes. I hope it will be illustrative of the potential of digital technology for tighter process monitoring.

Digital processing has permeated our daily lives in many ways. We communicate with each other digitally via cell phones and e-mail; read digital news on the internet; take digital photos and videos of our families; we will soon be watching digital TV. A decade ago, all of these media were analog - or didn't even exist. The reasons for the transformation are obvious to those of us who appreciate the power and flexibility of these toys. But "We," in Semiconductor Wafer Processing, are a bastion of Luddites. We love our analog signal processing, the noisier the better.

Take, for example, mass flow controllers. Analog MFCs are found everywhere in wafer fabs. They are used for metering precise quantities of reactive gases in many different types of equipment. Their performance and reliability are important determinants in our industry's ability to produce components with in-spec characteristics. Future processing - and safety - requirements will no doubt demand even more precise control and reliability in the metering of gaseous reactive chemicals than exists today.

Here are some reasons why I believe replacing analog components with their digital counterparts in current generations of fab equipment can help improve processes. First is "bandwidth and access." You can generate all the data you need to understand the subtleties of your equipment operation, without having to depend on a plodding SECS interface for data acquisition. This advantage becomes even more pronounced when process step times are measured in seconds. As an example, consider the many processes that depend upon maintaining a positive pressure gradient between two chambers during critical operations. If the equipment does not provide adequate monitoring and remedial action when error conditions occur, superimposing a digital pressure data monitoring system can.

A second reason is signal integrity (no noise), meaning you can easily use the digital data to dynamically track what a component thinks its setpoint is, and what it thinks its output is. Often this is quite different from what the equipment itself thinks. For example, MFC calibration problems frequently reveal themselves via a significant non-zero flow output signal when there is no gas flow. Yet, the process controllers on most current generation fab equipment are rarely programmed to look for this condition. In cases like this, where the existing equipment infrastructure is not able to deal with an identifiable problem, digital data monitoring systems can help add the needed intelligence to look for these conditions and initiate appropriate responses.

A third reason is that digital components come equipped with lots of Gadgets - just like cameras and cell phones - that improve their flexibility and usefulness over analog models. For example, you can instantly change their ranges, change the type of gas they can be used with, or automatically "tune" them to improve their performance under local conditions.

I used a test fixture consisting of a generic process controller, a bank of hybrid MFCs (equipped with both standard analog and digital interfaces), a "process chamber," and a vacuum system that crudely simulates a piece of process equipment such as a CVD system.

In this group of experiments, I tried to simulate the short-duration repetitive on-off cycling of gases that occurs in many different types of process equipment in use today in order to see what kinds of MFC problems high-bandwidth data capture might reveal. Nitrogen gas was introduced into a vacuum system at two-minute intervals, followed by an intervening minute with no flow. Trace data from a typical run is shown in Figure 1. This sequence was repeated several times.

Figure 1. Typical process run consisting of three "deposition" steps each followed by a pumpdown step.

Figure 2 shows some mean flow rate trends. There are three panels in this figure, each containing data from a different MFC. Each run is represented by three points (See Figure 1).

Figure 2. Mean flow trends for all three MFC used in the series of runs.

Note that there is substantial variation in the average flow rates of N2 from interval to interval. For the MFC in the upper panel, the average flow rate is 777 SCCM, 1-sigma is about 14 SCCM, and 3-sigma is 42 SCCM - about 5.4 percent. For the MFC in the center panel, 3-sigma is about 6 percent, and for the MFC in the lower panel - about 4 percent. Flow variations of this magnitude in process gases such as TEOS or SiH4 could possibly give rise to film non-uniformity of similar magnitude.

Figure 3 provides some insight into one of the possible reasons for the observed flow rate variations. This figure shows an overlay of the MFC trace data from several intervals. There is substantial variation. But does it account for the observed large standard deviations seen in Figure 2? Figure 4 shows the same trend results as in figure 2, but a 10-second delay in the start of the calculation was inserted. The standard deviations are lower in all cases, indicating that most of the observed flow variation from interval to interval occurs while the MFC is ramping up.Table I lists the means and standard deviations for all three flow controllers with and without the 10-second delay.

Figure 3. Trace MFC flow data overlay of five different intervals.  Note the variation as the MFC ramps up.

Figure 4. Sam summary process data as in Figure 2, but with 10-second delay before starting SPC calculation.

Table I
Flow Interval Mean and Standard Deviation Data
Calculated With and Without A 10-Second Delay

MFC Name Mean Del
1 sec
Std Dev Del 1 sec Mean Del
10 sec
Std Dev Del
10 sec
N2 1500 592 12.3 603 6.2
N2 1000 778 13.9 820 7.9
N2 75 43.6 0.58 43.0 0.43

Figure 5 shows a composite trace data plot of 15 flow intervals. The flow variations from interval to interval are striking. If anybody's real CVD systems exhibit flow profiles like those in the figure, I would think it might be worthy of some attention.

Figure 5. Trace data from several different runs.  Note the obvious differences in the flow data from interval-to-interval.

Figure 6 shows some other interesting trend data taken from the N2 1000 MFC. The top panel contains flow mean data for each interval, the lower panel contains valve voltage data. The data are seen to shift abruptly at about points 13 and 25. The flow rate shift at point 13 is about 2 percent. Figure 7 shows the same data, but the x-axis is plotted on a time scale. The abrupt changes are seen to occur after a time interval of several hours during which no processing was done. The explanation for the shifts is as follows: Since I'm using bottled Nitrogen, after each session I turned off the gas supply at the source to avoid having all my N2 leak away. When I turned it back on, I readjusted the input pressure to "something near 18 Psi", but the variations apparently produced a big shift in the valve voltage, and a measurable shift in flow.

Figure 6. Trend mean flow and value voltage data for the N2 1000 MFC. Note the abrupt shifts at points 13 and 25.

Figure 7. Same data as Figure 6, but x-axis represents time, rather than interval number.

Since time interval data are available, I thought it might be instructive to see what sorts of variations exist from interval to interval. Figure 8 shows some duration trend data. The average interval duration is 1.96 minutes - about four percent below the programmed interval duration of 2.0 minutes. Additionally, 1-sigma is .017 minutes, and 3-sigma is .051 minutes - 3 seconds. This represents a +/- 2.5 percent variation in interval duration among all the intervals measured. If you're trying to control film thickness down to the proverbial gnat's eyebrow, a 2.5 percent variation in the deposition time interval is just one more thing contributing to film non-uniformity.

Figure 8. Variation in interval duration for N2 1000 MFC.

Using a digital network, I was able to collect high-resolution flow data that illustrated several common types of MFC problems in gory detail. This was accomplished with a simple two-wire twisted pair network and a PC, and without touching any of our simulated tool's hardware infrastructure.

Whether the observed interval-to-interval flow variation during ramp-up is an MFC problem or some other equipment problem is immaterial - most MFCs, whether analog or digital, will experience problems sometime during their lifetimes. The point is that to fix problems you first have to be able to detect them, and to detect them you need the DATA.

Consider the litany of potential MFC problems: flow overshoots during setpoint changes, long settling times, unstable flow (oscillation), zero drift and calibration drift. MFCs function in a rugged environment; they are subjected to reactive and corrosive gases, and unstable pressure environments. It shouldn't surprise anyone that they break. The point is it's easier to spot one that's broken if it is a digital. I believe digital technology presents an opportunity to provide unprecedented automatic monitoring and detection of all sorts of subtle problems for hundreds of MFCs and other types of digitally equipped sensors throughout a wafer fab. Early Response systems are already in place in many fabs that automatically shut down process equipment when problems are encountered. Fault detection systems that utilize digital sensors can provide an extra measure of fab-wide early failure detection and intervention.

There are two potential channels for implementing digital technology in a wafer fab. One is through the OEMs who will incorporate digital components in future new equipment designs. This may happen on new-generation 300-mm equipment, but don't hold your breath waiting for OEMs to offer digital sensor retrofit kits. The other is for end-users to employ digital technology for their own use. This is actually fairly straightforward, because many components with digital interfaces are hybrids that can replace existing analog components. The networks are generally easy to install, usually requiring a simple two-wire twisted pair strung daisy-chain fashion from component to component, and a PC. There is no need to dig into the bowels of the tool's control system to install the network.

I believe digital technology presents an opportunity to provide unprecedented automatic monitoring and detection of all sorts of subtle problems for hundreds of MFCs and other types of digitally equipped sensors throughout a wafer fab. Early Response systems are already in place in many fabs that automatically shut down process equipment when problems are encountered. Fault detection systems that utilize digital sensors can provide an extra measure of fab-wide early failure detection and intervention.

* The Luddites were members of a Scottish movement opposed to the introduction of new weaving technology into the textile mills of the early 19th century. The name is sometimes loosely applied in modern times to those who express misgivings about today's new technology.

                                                                                                        

                                                                                                         


Copyright (c) 2006, Jon Goldman Associates


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