1. Field of the Invention
The present invention concerns a CO2 absorption device suitable for operation in an elemental analysis instrument, especially for nitrogen determination, particularly an instrument based on the Dumas method. Such an instrument consists of a high temperature sample combustion reactor with a current of oxygen, where the combustion gasses pass into a reduction reactor with the elimination of water, carbon dioxide and any SO2 present, prior to the gas being sent to a detector, particularly a nitrogen detector.
2. Description of the Prior Art
The use of chemical filters for CO2 elimination, which are simply replaced following a certain number of analytical cycles, are known in the art. However, such filters have a number of drawbacks, especially for high weight samples (for example 1-2 g of cereals) since the quantity of CO2 to be absorbed demands large filters, which have a negative impact on analytical performance. Furthermore, the reaction with large quantities of CO2 can be highly exothermic and lead to the curing of the absorbent material with increased load loss. The resulting increase in combustion reactor operating pressure reduces the conversion efficiency of the sample into elemental gas. Sending only a percentage of the combustion gas to the filter has been proposed as a solution for obviating such drawbacks, but this influences the accuracy and reproducibility of the analyses, and leads to further complications in the instrument pneumatics.
CO2 filters, acting at the physical level, which can be regenerated by means of heating and passing regenerative gas through, have also been proposed. In cases involving large quantities of CO2, such filters must necessarily also have large dimensions, and require long periods of time (of the order of 15 minutes) for their regeneration and subsequent cooling. Furthermore, it is practically essential to provide an upstream water filter, since the CO2 filter would absorb water more or less irreversibly, with consequential degradation of efficiency.
Patent application EP 1586895 illustrates an elemental analysis instrument envisaging a carousel with a number of regenerable CO2 filters, which are brought in succession into the operating position and then into the regeneration position. This solution allows reduced regeneration times, and the ability to move from one analysis to the next without pausing. However, there are problems with the pneumatic seals and, in the case of heavy samples, the device requires individual, large sized filters and therefore has a tendency to be excessively bulky.
The scope of the present invention is therefore that of providing a device for absorbing CO2, intended for use in an elemental analysis instrument, that is both regenerable, capable of operating without any moving parts, with high efficiency, and does not require any time for regeneration between one analysis and the next, even for high weight samples.
These scopes, and others, which will become evident from the following description, are achieved by a CO2 absorption device according to claims 1 to 16 operating in an elemental analysis instrument according to claims 17 to 20.
The device and the instrument according to the invention will be described with reference to a preferred embodiment, illustrated schematically, purely by way of non-limiting illustration, in the attached figures, in which:
The diagram in figure
A water condenser 24 is fitted to the line 22 in order to remove condensed water, and discharge it externally by means of line 25. Line 22 then feeds gas to the device 26 which handles the absorption of the CO2, any remaining water and any SO2, if present
The device 26 has two filters, one involved in the absorption stage and one undergoing regeneration by means of heating and passing through a regenerating gas, which may be the same helium carrier, supplied and exhausted by means of line 27. A gas chromatography column 28 and a detector 29, to which a reference gas is also supplied by means of line 30, are arranged downstream in the known manner.
The device 26 is shown schematically in
It should be observed that the pneumatic connections shown operate in such a way that filter regeneration always occurs with a flow of carrier in the opposite direction with respect to the flow of gas during the absorption stage for the same filter. This is very important since, as will be appreciated below, it allows improved regeneration conditions, and hence improved device operating conditions.
In
In the first position shown in
With reference to
The interior volume of the tube is filled with a packing composed of one or more CO2-absorbent materials arranged and/or selected so as to provide a CO2 absorbent power that increases from the filter inlet to the filter outlet in the direction, marked X, taken by the gas during the analysis stage. In particular, said material may be comprised of molecular sieves with granulometry that decreases from the inlet to the outlet in the aforementioned direction, in particular, for example, two different granulometries, as shown the larger in 53 and the finer in 54, respectively.
Still in the direction undertaken by the gas undergoing analysis, upstream of the CO2-absorbent material is preferably positioned an absorbent material 55 for any H2O not retained by the condenser 24, and upstream of this latter item at least one SO2-absorbent material 56 may be optionally positioned. This layout of the materials making up the filter considerably aids the regeneration stage, which, as already mentioned, occurs with the flow in the opposite direction, so that, during regeneration, any SO2 and water do not pass through, and therefore have no effect on the CO2-absorbent materials. The latter are then treated by the flow of regenerating gas in such a way that the fresh gas first comes into contact with the areas most loaded with CO2 then little by little moving onto the least loaded areas, towards the end of its path. This improves the regeneration conditions and effects which, thanks also to the other construction details of the filter and its reduced thermal mass, may be completed and the filter cooled within a very short period of time, typically between 3 to 8 minutes.
A fan assists with speeding up the filter cooling process, in order to complete the regeneration process in times that are essentially equal to those required for analysis.
Number | Date | Country | Kind |
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MI2006A 000813 | Apr 2006 | IT | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2006/002455 | 9/5/2006 | WO | 00 | 1/30/2009 |