As illustrated in
The flow tube or flow drift tube 6 is generally held at a pressure of approximately 0.5 to 1.0 Torr and a stream of a non-reactive carrier gas or gas mixture, typically helium is injected at 8 into the flow tube in a manner that a venturi effect is obtained to prevent the ion stream from the chamber 1 and the non-reactive gas from escaping back into the upstream chamber. Additional non-reactive carrier gas or mixture of non-reactive gases, can be injected at additional points along tube 6.
The sample of the volatile organic compound (VOC) is injected at 7 into the flow tube and reacts with the incident beam of ions, the result of which is a transfer of ions to the VOC. The charged VOCs then enter the downstream chamber through a small injection orifice 11 with the downstream chamber 10 generally held at a similar pressure (106 Torr) to the upstream chamber 1. As in the case of the upstream chamber, the downstream chamber 10 is normally evacuated by means of a turbo pump 12 or similar. The downstream chamber includes a set of lenses 13 and a quadrupole mass filter 14 with a detector device 15 by which the masses of the incident VOCs and precursor ions are measured. Backing pumps are shown at 16 and these allow the chambers 1 and 10 to be evacuated sufficiently to allow turbo pumps 12 to maintain the desired chamber pressure.
In the following description and claims the term “flow tube” is intended to include both a flow tube and a flow drift tube.
The improved SIFT-MS or SIFDT-MS instrument is illustrated diagrammatically in
Depending on the source of ions and the construction of the chamber various undesired particles may enter the chamber and depending upon the type of particles it can be necessary to insert an electrostatic shield in the chamber to block these particles from reaching the detector. As illustrated in
The pump 21 must be chosen to ensure both sides of the shielded chamber are adequately pumped to allow the quadrupole mass filters 22 and 29 and also the detector to operate within their required ranges. It will be understood that if the shield is constructed from a metal grid or gauze, then the pumping will be arranged to take into account the possible permeability of the shields. Backing pumps are shown at 26 and these allow the chamber 20 to be evacuated sufficiently to allow the pumping system 21 to maintain the desired chamber pressure.
As in the case of the instrument illustrated in
Because of the improvements in the instrument brought about by the present invention, it is possible to make the whole instrument considerably physically smaller with less componentry that that previously required. This provides significant savings in the cost in the manufacture of the instrument. In addition, because only a single pump is used, less electrical power is required and less noise is generated. This reduces the considerable amount of sound insulation that was previously required. It is to be understood this is a major advantage when constructing the instrument as a portable instrument because this will result in a reduction of the number of component parts and consequently in the size of the machine and in the weight of the machine
Having described the preferred embodiments of the invention it will be apparent to those skilled in the art that various changes and alterations can be made to the embodiments and yet still come within the general concept of the invention. All such changes and alterations are intended to be included in the scope of this specification
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/NZ04/00297 | 11/24/2004 | WO | 00 | 5/23/2006 |