ISO 609-1996 Solid mineral fuels - Determination of carbon and hydrogen - High temperature combustion method《固体矿物燃料 碳和氢含量的测定 高温燃烧法》.pdf
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1、INTERNATIONAL STANDARD IS0 609 Second edition 1996-02-I 5 AN251 IBPntemat Dot se!c Solid mineral fuels - Determination of carbon and hydrogen - High temperature combustion method Combustibles minkaux solides - Dosage du carbone et de Ihydrogene - MBthode par combustion B haute tempkrature - - 1 gffi
2、 1 k sodium hydroxide on an inert base (4.2) for ab- sorbing dioxide; magnesium perchlorate for absorbing the water evolved in the reaction between carbon dioxide and sodium hydroxide. The purification trains shall be large enough to render frequent recharging unnecessary, even with continu- ous use
3、. NOTE 1 Midvale tubes that have been freshly packed with absorbent and used in the purification train are thereby conditioned for subsequent use in the absorption train. 5.4 Combustion assembly 5.4.1 Heating unit, an electrically heated furnace or furnaces, designed to carry a combustion tube (5.4.
4、2) and heat it to 1 350 “C over a distance of 125 mm in the hot zone, and yield a temperature-distribution profile similar to that shown in figure 1. The heating unit normally requires an auxiliary furnace to ensure that the silver gauze roll (5.9) is maintained at the correct temperature (approxima
5、tely 600 “C to 800 “C). Suitable furnaces are, for example: a) molybdenum or tungsten wire wound; b) platinum or platinum-rhodium wire wound; c) heated by silicon carbide rods. , IS0 609:1996(E) NOTES 0 100 200 300 400 500 600 Distance from inlet end. mm 75 mm Combustion tube / / /% Silver gauze rol
6、l Heat-resistant mineral fibre / Figure 1 - Typical temperature-distribution curve for furnace deep for brown coal and lignite, capable of with- 2 Type c) has the lowest initial cost and has proved satis- factory in use. 3 Furnaces of the type normally used for the determi- nation of carbon or sulfu
7、r in steel are not suitable because of the absence of the auxiliary section required to maintain the silver gauze roll at the correct temperature. 5.4.2 Combustion tube, of approximately 28 mm external diameter, 3 mm wall thickness and 650 mm length, made of refractory aluminous porcelain which is i
8、mpervious to gases up to a temperature of 1 400 “C. The end of the combustion tube shall be lagged with a suitable heat-resistant mineral fibre to prevent condensation in the tube. 5.4.3 Combustion boat, of iron-free, unglazed porcelain, approximately 60 mm long, 12,5 mm wide and 10 mm deep, for har
9、d coal and coke samples and approximately 75 mm long, 15 mm wide and 10 mm standing a temperature of 1 350 “C. NOTE 4 Combustion boats should not blister, discolour or change in mass on heating in oxygen at 1 350 “C for 3 h. A suitable boat lasts for about IO to 20 determinations and should then be
10、discarded because of the accumulation of fused ash. For coals with a high ash content, it may be convenient to line the boat with alumina before adding the sample, in order to prevent fusion of the ash to the boat. 5.5 Absorption train, for absorbing the water and carbon dioxide evolved by the combu
11、stion of the sample. Midvale tubes (figure21, which provide a large area of reaction, are used in order to reduce the back-pressure in the apparatus, and so obviate the danger of leakage through the rubber sleeve carrying the pusher. Assemble the train using the following reagents in the order state
12、d, in the direction of flow: a) magnesium perchlorate (4.1) for absorbing the water evolved during the combustion; 3 IS0 609:1996(E) 0 IS0 Dimensions in millimetres Indicator spot - 0 ext. 5.5 to 6 0 ext. 33 to 34 Wall thickness 1 to 1.25 .5 to 6 Figure 2 - Midvale tube b) sodium hydroxide on an ine
13、rt base (4.2) for ab- sorbing carbon dioxide; c) magnesium perchlorate for absorbing the water evolved in the reaction between carbon dioxide and sodium hydroxide. Place glass wool (4.101, previously dried at 105 “C for 1 h, above and below the absorbents to prevent the carry-over of dust by the flo
14、w of oxygen, and to pre- vent the cracking of the Midvale tube by the heat of reaction. A typical absorption train with details of the packing is shown in figure3. A is the absorber for water; B and C are the absorbers for carbon dioxide, C serving as a control to indicate when the packing in B is i
15、n need of replacement. Any water released in B by the reaction between sodium hydroxide and car- bon dioxide is absorbed in C. The inlet of the water-absorption tube shall be in- serted through the heat-resistant stopper so that it is flush with the inner end of the stopper. All con- nections betwee
16、n the tubes shall be made of glass- to-glass, using the rubber connecting sleeves merely as seals. 4 IS0 609:1996(E) 4- 3- Key 1 Glass wool 3 Magnesium perchlorate, I,2 mm to 0.7 mm size 2 Sodium hydroxide (see 4.2) 4 Inlet Figure 3 - Absorption train 5.6 Two flowmeters, both capable of measuring ra
17、tes of flow up to 300 ml/min of air. 5.7 Heat-resistant stopper (acrylonitrile or chloroprene) for connecting the absorption train to the combustion tube. 5.8 Silica or steel pusher, made from rod or sealed tube, approximately 6 mm in diameter and 450 mm long, with a disc end, 12 mm in diameter, for
18、 pushing the boat into the hot zone of the combustion tube. The pusher passes loosely through a glass or metal T-piece, one end of which fits into the stopper which closes the inlet end of the combustion tube, the other being sealed by a rubber sleeve (see note 61, through which the pusher slides. T
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