An area of increasing development in the field of gas chromatography (GC) is instrument miniaturization. Notable examples of such advances include portable field GC units and GC separations achieved on a micro-analytical chip. In conjunction with these efforts, there is also a growing interest in developing sensitive miniaturized detection methods that can be incorporated into micro-analytical devices. A number of such miniaturized or ‘micro’ detection methods have been reported based on a variety of principles including surface acoustic wave transmission, thermal conductivity, and plasma-based optical emission. Although flame-based detectors are prevalent in many conventional GC applications, relatively few have been adapted to micro-analytical formats. Since the latter tend to utilize very small (nL range) channels, this may be partly attributed to difficulties encountered in operating a stable flame within these dimensions. In this regard, however, a very interesting and useful system has been successfully demonstrated. The method employs low gas flows to support a high energy premixed flame (about 3 mm tall×1 mm wide) that can perform atomic emission/hydrocarbon ionization detection on the surface of a micro-analytical chip.
The flame photometric detector (FPD) is a widely used GC sensor for determining sulfur, phosphorus, tin, and other elements in volatile organic compounds based on their chemiluminescence within a low-temperature, hydrogen-rich flame. We introduced a novel method of generating a similar flame environment using counter-flowing streams of gas [K. B. Thurbide, B. W. Cooke, W. A. Aue, J. Chromatogr. 1029 (2004) 193.]. This ‘counter-current’ FPD was demonstrated to provide similar sensitivity and response characteristics to that of a conventional FPD when operated in the hydrogen-rich mode. As well, it was also found to yield useful flame ionization detector (FID) signals when operated in the air-rich mode. Most notably, unlike a conventional FPD, this method produced remarkably stable flames at relatively low and high gas flows of varying stoichiometry. In fact, this aspect of the detector was employed in the primary focus of the study, which explored changes in transition metal response as a function of flame size derived from gas flows that differed by several hundred mL/min.
Subsequent to this work (but reported earlier) we exploited the great stability of counter-current flames in a new way by using them to create an enclosed hydrogen-rich micro-flame [K. B. Thurbide, C. D. Anderson, Analyst 128 (2003) 616]. The flame was supported on a fused silica capillary by only a few mL/min of gas flow and encompassed a very small volume of 30 nL. As well, it produced qualitatively similar response characteristics toward sulfur and phosphorus-containing analytes as that of a conventional FPD. The method was employed in a novel micro-Flame Photometric Detector (μFPD) which was operated either inside the end of a capillary gas chromatography column (on-column) or within a length of capillary quartz tubing after the separation column (post-column), with each mode displaying similar characteristics.
In general, the dimensions and qualities of the micro counter-current flame indicated that it could be a potentially useful method of producing chemiluminescent molecular emission, similar to a conventional FPD, within small channels and analytical devices of reduced proportions. However, unlike the larger counter-current flame, the primary disadvantage to the micro-flame method was the relatively large detection limits that it produced for sulfur and phosphorus due to an elevated background emission. The spectrum, intensity, and orange appearance of the emission indicated that the fused silica capillary burner was glowing from contact with the flame. Despite efforts to prevent this it was observed under all conditions investigated.
A flame detector is described in the parent application, which is U.S. Application Publication No. 2005/0287033 published Dec. 29, 2005 (the '033 Publication), in which a micro-flame detector is provided comprising a housing having an oxygen inlet, a hydrogen inlet, an analyte port and a flame region. A metal capillary delivers oxygen through the oxygen inlet to the flame region. The metal capillary has a melting point sufficiently high that glow emissions from the metal capillary during flame detection does not significantly interfere with detection. A hydrogen and analyte delivery system delivers hydrogen and analyte to the flame region. The flame detector may be operated in a photometric mode in which a photo-detector is arranged to detect flame emission through a flame detection port or an ionization mode in which an ionization detector is arranged to detect flame characteristics. In an embodiment, the metal capillary provides a flame stabilization surface for a flame less than 1 μL in volume. In another embodiment, the metal capillary is a stainless steel capillary. The hydrogen and oxygen may be provided in a countercurrent mode.
The results reported in the '033 publication for the μFID were generated as a by-product of the hydrogen-rich flame conditions designed to promote chemiluminescence and photometric detection of target analytes in the μFPD. The μFID may be used as an independent detector for use in GC. For example, the μFID may be operated inside the end of a capillary GC column. Subsequently, within similar greatly reduced dimensions, an oxygen-rich μFID operating mode is also disclosed where the micro counter-current flame is situated on the end of a hydrogen-delivering capillary immersed in an opposing excess oxygen flow.
Therefore, there is disclosed a micro-flame detector, comprising a first tube connected to an oxygen source and providing a flow path for oxygen towards a flame region; a second tube connected to a hydrogen source and providing a flow path for hydrogen towards the flame region; the first tube and second tube being arranged to provide counter-current flows of oxygen and hydrogen in the flame region; at least one of the first tube and the second tube being a metal capillary terminating at the flame region and having a melting point sufficiently high that glow emissions from the metal capillary during flame detection does not significantly interfere with detection; a source of analyte leading to the flame region; the metal capillary providing a flame stabilization surface for a flame less than 1 μL in volume; and at least a detector arranged about the flame region, the detector comprising at least one of an ionization detector and a photodetector. In one embodiment, the flame stabilizes on the hydrogen delivery tube, and in another embodiment, on the oxygen delivery tube. In a further embodiment, the flame is established immediately on top of a GC column. Methods of operating a micro-flame detector are disclosed. Various other embodiments are described below and claimed.
There will now be described preferred embodiments of the invention by reference to the figures, by way of illustration only, in which:
In this patent document, the word “comprising” does not exclude other elements being present and the use of the indefinite article “a” before an element does not exclude others of the same element being present. A flame photometric detector is considered to be a micro-flame detector, either μFID (ionization detector) or μFPD (photometric detector), if the flame volume, as defined by the visible boundary of the flame, is less than 1 μL (1×10−6 L), which for example is satisfied by spherical flame diameters of less than 1 mm. In particular, the μFPD shown in
A micro-flame detector arranged for counter-current operation comprises a first tube connected to an oxygen source that provides a flow path for oxygen towards a flame region and a second tube connected to a hydrogen source that provides a flow path for hydrogen towards the flame region, the flows being opposite to each other in the flame region. At least one of the first tube and the second tube is a metal capillary that terminates at the flame region. The metal capillary has a melting point sufficiently high that glow emissions from the metal capillary during flame detection does not significantly interfere with detection. The flame region will typically be protected from interference from outside sources by for example being defined within a larger sleeve, for example made of quartz. The metal capillary should be small enough to provide a flame stabilization surface for a flame less than 1 μL in volume (the flame volume being defined by that portion of the flame that emits light in the visible spectrum). A source of analyte leads to the flame region, as for example a GC column. The analyte may also be provided through a separate tube, or through the hydrogen delivery tube or through the oxygen delivery tube, and need not be sourced from a GC column. A detector is arranged about the flame region to detect properties of the flame. For photodetector operation, a photodetector is arranged about the flame region, and for ionization detection, the collector of an ionization detector is arranged about the flame region.
The separation column 20 extends vertically upward from the GC instrument and into the detector housing 10 through the connecting stainless steel tube 22 carrying the hydrogen. Typical separations employ 5 mL/min of helium as the carrier gas. In an embodiment, about 1-3 mm separates the end of the column 20 from the oxygen burner 38. For μFID experiments, electrical leads from a gas chromatograph (GC) are used such that the polarizer 44 of the GC is connected to the stainless steel oxygen burner 38 and the collector 46 is connected to the stainless steel hydrogen tube 22 surrounding the separation column 20.
Stainless steel is an improvement over fused silica because it has a higher heat capacity. As such, the heat of the flame does not cause it to glow from being incandescently heated. Glowing creates a large background response in the detector, which decreases its sensitivity. The improvement offered by stainless steel includes improved detection limits and the simultaneous FID method, and allow the method to be useful in more situations. In addition to a stainless steel capillary, the flame could also be supported on other metals that have a sufficiently high melting point, such as nickel, or some alloys. Typical flame volume for the stainless steel shown in
To light the device, the oxygen containing capillary 38 is drawn through a flame, ignited, and is pushed into the hydrogen stream, keeping it lit. The original flame either extinguishes or can be blown out like a candle. Once lit, the flame 42 generally stays stable for hours. Use of pure oxygen is preferred as a supply of oxygen. Various flow rates may be used depending on the arrangement. Thus, in one embodiment described in the '033 publication, a lower hydrogen limit measured was 6 mL min−1 using 2 mL min−1 of oxygen while the upper hydrogen limit measured was 113 mL min−1 using 5 mL min−1 of oxygen. In the embodiment disclosed in the '033 publication, the optimal flow region for operation was found to be in the area of 6 mL min−1 of hydrogen and 2 mL min−1 of oxygen. This flow region did not display any signs of flame instability and was typically operated daily for over 8 h with no degradation in performance. Lower gas flows than 6 mL min−1 of hydrogen and 2 mL min−1 of oxygen are also believed to provide flame stability.
Stainless steel capillary tubing of 0.01″ i.d., (0.018″ o.d., wall thickness of 0.004″) used as a burner 38 in the example of
The use of a stainless steel capillary burner 38 makes it very convenient to apply a potential across the flame using the existing FID electrical leads of a GC, as for example by applying the polarizer 44 to the capillary burner 38 and the collector 46 to the stainless steel sleeve 22 surrounding the end of the separation column. In the ionization configuration, when the capillary burner was new, about 12 mL/min of oxygen was found to provide the best sensitivity. However, after a few hours of conditioning, this value decreased and stabilized at lower flows. Ultimately, the optimum gas flows for the “μFID” response mode of this flame toward carbon were obtained using 7 mL/min of oxygen and 40 mL/min of hydrogen. As disclosed in the '033 publication, the FID configuration of the device shown in
In the example shown in
For the results described below, test analytes used for calibrations and applications are benzene (99%; EM Science, Gibbstown, N.J., U.S.A.), decane (99%; BDH Lab Supplies, Toronto, Canada), cyclopentanol (99%; Matheson Coleman & Bell, Cincinnati, Ohio, USA), naphthalene (99%; Fisher Scientific Company, Fair Lawn, N.J., USA), and tetradecane, hexadecane, octadecane, and eicosane (each 99%; Aldrich, Oakville, Canada). A commercial Norpar paraffin distillate (undecane (1%), dodecane (19%), tridecane (47%), tetradecane (32%), and pentadecane (1%)) acquired from the Petroleum Engineering Department on campus is also employed in some demonstrations. Samples were made by dissolving varying concentrations of the desired solutes in either acetone (99.5%, EMD Chemicals, Gibbstown, N.J., U.S.A.), carbon disulfide (99%; EMD chemicals), or hexane (analytical reagent; BDH Lab Supplies). Finally, a BTEX mixture (benzene (185 ng/μL), toluene (186 ng/μL), ethyl benzene (196 ng/μL), and xylenes (396 ng/μL meta/para combined, and 200 ng/μL ortho)) is also used as obtained from Dow Chemical (Fort Saskatchewan, Canada). Separations are performed on an EC-5 [(5%-phenyl)-95% methylpolysiloxane] megabore column (30 m×0.53 mm I.D.; 1.00 Mm thick, Alltech, Deerfield, Ill., USA) and normally use approximately 5 mL/min of high purity helium (Praxair, Calgary, Canada) as the carrier gas. High purity hydrogen (Praxair) is used as the flame fuel gas and, in some experiments, also the carrier gas. Medical-grade oxygen (Praxair) is used as the flame oxidant gas. Flow rates are discussed in the text.
An on-column μFID arrangement used for the results described here is depicted in
For the results described here, used with a retrofitted GC, the flame 70 was slowly moved along the inner wall of the GC column outlet 66 in order to burn off carbonaceous stationary phase and prevent it from interfering with the μFID response. An outer polyimide coating was also removed in this process. The flame 70 may be established at various levels within the GC column outlet 66, and in the case of a retro-fit, a sufficient distance from column coating to avoid further combustion of stationary phase, as for example 2.5 mm ahead of the remaining GC column coating. While the flame could be easily positioned at any depth inside of the GC column 56, it may for example be situated about 5 mm (>10 flame diameters) inside the outlet. This ensured that the flame 70 was completely enclosed on all sides and that all of the column effluent was directed through it. This position was also optimal in keeping the flame 70 in reasonable proximity to the collector 62 coiled around the column outlet 66. Minimizing this distance was essential to operation of this specific embodiment since preliminary trials using a BTEX sample indicated that too great of a flame-collector gap was observed to cause the μFID signal intensity to approach zero and the reproducibility to degrade significantly (e.g. from ˜2% to over 17% RSD). A collector that is located too far from the flame region is thus non-functional as an FID detector, and it is assumed, when a detector is referred to, that it is located in sufficient proximity to the flame region 72 to detect a signal.
In optimizing the flame gas flows for carbon response, for the specific embodiment shown, it was found that the hydrogen fuel/carrier gas needed to be above 8 mL/min to facilitate separation, even though lower hydrogen flows could readily support a stable flame. Optimal conditions will depend on the specific embodiment used, but for the design of
The findings above suggest that a dedicated on-column μFID format should offer some potential advantages in certain GC applications. For example, its compact enclosure could minimize the spatial requirements of an on-board detector in micro-analytical devices that are constrained by extremely small dimensions. Additionally, the reduced gas flow requirements could increase operating lifetimes and decrease the amount of portable supply gas needed in field trials. Alternatively, the on-column μFID mode may also be useful in high speed GC separations, which often similarly employ hydrogen as the carrier gas through a capillary column. For example, it could further reduce supply gas requirements by eliminating the need for large makeup gas flows that are normally used in these methods to minimize critical extra-column peak broadening occurring en route to the detector. However, with respect to the latter application, it is worthwhile to also briefly address some other μFID properties relevant to its adaptability in this regard.
The conventional FID is widely used in fast GC applications partly due to its rapid response, which allows it to effectively profile the relatively narrow peaks generated by these techniques. As part of the current study, the detector time constant of an on-column μFID, a post-column μFID, and a conventional FID were estimated and compared using standard protocol. In fact, little difference was observed in the values obtained, which were all within the low millisecond range similar to that reported for a conventional FID. Another favorable property of the conventional FID in this area is its sturdy flame operation in the presence of high carrier gas flow rates, which are also frequently used in fast GC separations. Similar to earlier counter-current flame studies, it was additionally found in this work that the μFID flame also remains very stable as carrier gas flow rates are increased from relatively small to very large values. For example, using only 4 mL/min of oxygen, the on-column μFID could readily function with hydrogen flow rates of over 100 mL/min. Comparable results were also obtained when using helium as the carrier gas in a post-column μFID configuration. Thus, despite the different size and nature of their respective counter-current and diffusion flames, no difference in response time or flame stability is to be expected between the μFID and a conventional FID in such applications.
Although the on-column μFID mode provides a favorable flame size and stability using relatively low gas flows, its response characteristics are the same as those of the original device disclosed in the '033 publication. This is because the on-column μFID is still maintaining a slightly hydrogen-rich micro counter-current flame, as opposed to the largely oxygen-rich diffusion flame of a conventional FID. In optimizing the on-column μFID mode, it was found that using even larger flows of oxygen lifted the flame off of the capillary burner and dramatically decreased the response due to ineffective flame polarization. Thus, it was decided that it would be interesting to utilize the small dimensions of the on-column format but in a post-column μFID device. The anticipation was that this might enable the use of similar reduced gas flows while also allowing, for the first time, an oxygen-rich micro counter-current flame to be operated in attempts to improve sensitivity.
Previous work with much larger counter-current flames has shown that stability can be maintained over a wide range of flame stoichiometry when using opposing burner arrangements. For example, in this larger format the flame normally resides on the burner delivering the limiting reagent gas, where under stoichiometric conditions it often hovers between the burners without making contact. However, previous attempts to operate an oxygen-rich micro counter-current flame in the dedicated μFPD arrangement was noted to result in unstable conditions due to the burner and quartz sleeve used. Therefore, this was expanded upon in the current study.
As shown in
Since the flame enclosure was about the same diameter as the on-column mode, the optimal hydrogen flow rate in the inverted mode of
The on-column and inverted μFID operating modes developed and investigated in this study further demonstrate that stable, low-flow micro counter-current flames of varying stoichiometry can be established within small enclosures and can produce valuable μFID response. While the findings indicate that further reductions in the size of the burner and flame enclosure might lead to even lower operating gas flows, the impact of such an endeavor on flame stability and response remains unknown. In general, therefore, despite the minuscule unique structure of the counter-current flame, the overall results from using this approach indicate that response characteristics similar to those of larger analog GC detector flames can be obtained by this method. As such, these properties suggest that the developed micro counter-current flame detection method may be useful for adaptation to portable and micro-analytical GC applications.
The apparatus and method disclosed here should also act as a useful flame source to support and adapt other micro-flame based detection methods such as Alkali Flame Detection. The apparatus and method disclosed also have utility in refinery and hydrocarbon processing plants for example in online applications. In addition, by adjusting the flow rate of hydrogen and oxygen, the flame may be made to stabilize between the oxygen delivery tube and the hydrogen delivery tube. In this case, the tubes define a flame stabilization region between them, and in order to provide a useful signal, depending upon the detection system used, the flame should be polarized by other means, such as by using a separate electrode (not shown) extending into the flame region. In cases where the flame is stabilized between the burners and separated from the burners, but not touching either burner, a metal capillary need not be used, and both burners may for example be made of glass. While embodiments have been disclosed in which counter-current flows are directly opposed to each other, counter-current flows may also be offset from direct opposition, providing the lateral flow of gas induced by the offset does not de-stabilize the flame. Further, while pure oxygen is preferred, the oxygen flow, and also the hydrogen flow, may include other gases providing the flow is sufficient to produce a flame without significantly degradating the signal from the flame emission.
Immaterial modifications may be made to the embodiment of the invention described here without departing from the invention.
This application is a continuation-in-part of U.S. patent application Ser. No. 11/109,017 filed Dec. 22, 2004, and claims the benefit under 35 USC 119(e) of U.S. Provisional Application No. 60/582,549 filed Jun. 25, 2004. Both of these applications are incorporated by reference herein in their entirety.
Number | Date | Country | |
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60582549 | Jun 2004 | US |
Number | Date | Country | |
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Parent | 11019107 | Dec 2004 | US |
Child | 11946788 | US |