ISO 6326-5-1989 Natural gas determination of sulfur compounds part 5 Lingener combustion method《天然气 硫化物的测定 第5部分 林格聂尔燃烧法》.pdf
《ISO 6326-5-1989 Natural gas determination of sulfur compounds part 5 Lingener combustion method《天然气 硫化物的测定 第5部分 林格聂尔燃烧法》.pdf》由会员分享,可在线阅读,更多相关《ISO 6326-5-1989 Natural gas determination of sulfur compounds part 5 Lingener combustion method《天然气 硫化物的测定 第5部分 林格聂尔燃烧法》.pdf(16页珍藏版)》请在麦多课文档分享上搜索。
1、INTERNATIONAL STANDARD ISO 6326-5 First edition 1989-07-01 Natura1 gas - Determination of Sulfur compounds - Part 5 : Lingener combustion method Gaz naturel - Determination des composh soufr 101,325 kPa). 4 Reagents and materials 2 Normative rederences The following Standards contain provisions whic
2、h, through reference in this text, constitute provisions of this part of ISO 6326. At the time of publication, the editions indicated were valid. All Standards are subject to revision, and Parties to agreements based on this part of ISO 6326 are encouraged to investigate the possibility of applying
3、the most recent editions of the Standards listed below. Members of IEC and ISO main- tain registers of currently valid International Standards. ISO 385-1 : 1984, Laborstory glassware - 5urettes - Part 7 : General requiremen ts. ISO 648 : 1977, Laborstory glassware - he-mark pipettes. ISO 1042 : 1983
4、, Laboratory glassware - One-mark volume tric flasks. ISO 3585 : 1976, Glass plant, Pipeline and fittings - Properties of borosilicate glass 3.3. During the analysis, use only reagents of recognized analytical grade and only distilled water or water sf equivalent purity. 4% Hydrogen Peroxide, IO % (
5、rnlrn) aqueous Solution, Sulfur-free, as absorbing liquid for the Sulfur oxides. 4.2 Activated carbsn, for adsorption of Sulfur impurities from the combustion air. 4.3 Absorbing liquid : 30 % Onln) aqueous Solution of potassium hydroxide, for the purification of the combustion air. 5 Apparatus The s
6、chematic layout of the apparatus is shown in figure 1. Ordinary laboratory apparatus and ISO 6326-5 : 1989 (El Air Figure 1 - Schematic layout of the apparatus Combustion device Pressure-equalizing vessel Capillary flow meter U-tube manometer Dry gas meter with thermometer Condensate separator Vacuu
7、m pump 5.1 Combustion device (AI The combustion device is manufactured of borosilicate glass complying with ISO 3535. lt consists of the Parts shown in figure 2, 5.1.1 Receiver with cooling jacket (see figure 3). 5.1.2 Flame tube (see figure 4) The outer diameter of the flame tube is determined by t
8、he in- side diameter of the receiver with cooling jacket and the annular gap shown in figure 2. 5.1.3 Burner (see figure 5) For the combustion of natura1 gases a universal burner with a needle valve is often preferable. 5.1.4 Intermediate piece (see figure 6) The thermometer shall have a measuring r
9、ange of 0 OC to at least 100 OC. The scale interval shall be not less than 1 OC. 51.5 Reitmeyer attachment (see figure 7). 5.2 Pressure-equaliming vessel (BL 5.3 Capillary flow meter (C), measuring range 10 I/min to 30 I/min. 5.4 U-tube manometer (D), arm length 500 mm. 5.5 Dry gas meter (E) The ran
10、ge of the meter shall be appropriate for the quantity of Sample to be burned and the meter shall have been recently calibrated. The gas meter shall be equipped with a thermometer for the measurement of the gas temperature. The thermometer shall have a measuring range of 0 OC to at least 30 OC. The s
11、cale intervals shall be not less than 0,5 OC. NOTE - The gas meter should be flushed with the gas to be analysed before the combustion, in particular when analysing gases with dif- ferent Sulfur contents, to avoid disturbance by adsorption and desorp- tion phenomena. 5.6 Condensate separator (FL 5.7
12、 Vacuum pump (GI The suction capacity of the vacuum pump shall be at least 25 I/min. lt is recommended that a drying tower with a drying agent be included between the condensate separator (F) and the vacuum pump (G) to protect the oil in the vacuum pump. 2 ISO 6326-5 : Dimensions in millimetres 1989
13、 (E) Tube8x l- Tube 10 x l- 3,2o,z Annular gap II I I II I 1 11 I I Il I I II I I I II I 11 I I Il ll l Ir 1 I I I I I h l ek l I I 11 / I 11 I 11 I 11 Ii 1 JI * /- Centred flame-tube Figure 2 - Combustion vessel ISO 6326-5 : 1989 (E) Dimensions in millimetres Dimensions in millimetres Conical joint
14、-socket 60/46 Spherical joint-cup 29/ 15-, Hose connectionY C 2 f 0 s / iTube54x 1,8 Tube 75 x 2,2 Conical joint- r / Eight holes 2+ir5 - uniformly distributed over the periphery / / r, 1 socket 45/40 socket 45/40 L Conical joint- cone 60146 Conical joint- cone 60146 Tube 40 x 1,6 Tube 40 x 1,6 Tube
15、44x 1,6 LOne-way cock Figure 3 - Receiver with cooling jacket Figure 4 - Flame tube ISO 6326-5 : 1989 (El Dimensions in millimetres 50 Spherical joint-cup- k-4 13112 Three apertures f-q 9,5 k 0,5 Gas jet apertu 0,l + 0,05 . Tube4Oxl Extension displaced rearward by 90 - ,6- 79n-Y Spherical joint-cup-
16、 1 1919 Conical joint-cone / 45/40 Tube 1Ox l- / Figure 5 - Burner Figure 6 - Intermediate piece Dimensions in millimetres iV- Thermometer Spherical joint-ball- 29115 Dimensions in millimetres i- Bent rearward through 90 Conical joint- socket 14/23 A -0 + 00 -8 joint-socket 14/23 Spherical joint-cup
17、 29115 Spherical joint-ball 29/15i Figure 7 - Reitmeyer attachment 5 ISO 6326-5 : 1989 (El 6 Procedure 61 . Preparation for combustion Draw air, which if necessary should be cleaned of Sulfur im- purities with activated carbon (4.2) and/or absorbing liquid (4.31, through the combustion apparatus wit
18、h the aid of the vacuum pump (GI, with a required volumetric flow about 20 I/min. Remove the burner (5.1.3) and pour sufficient hydrogen peroxide Solution (4.1) into the receiver (5.1.1) to rise around the flame tube (5.1.2) to the height of the burner tip throughout the period of combustion. After
19、connection of the cooling water, the combustion apparatus is ready for use. 6.2 Combustion With a preliminary pressure of about 2 kPa on the U-tube manometer (D), ignite the gas at the removed burner. Carefully introduce the burner, with the flame directed downwards, into the flame tube and note the
20、 reading on the gas meter (EI. The air flow and cooling water flow may have to be adjusted. The temperature and pressure of the gas shall be read during the combustion period. The exhaust gas temperature on the ther- mometer shall be kept between 50 OC and 70 OC. As soon as the required quantity of
- 1.请仔细阅读文档,确保文档完整性,对于不预览、不比对内容而直接下载带来的问题本站不予受理。
- 2.下载的文档,不会出现我们的网址水印。
- 3、该文档所得收入(下载+内容+预览)归上传者、原创作者;如果您是本文档原作者,请点此认领!既往收益都归您。
下载文档到电脑,查找使用更方便
10000 积分 0人已下载
下载 | 加入VIP,交流精品资源 |
- 配套讲稿:
如PPT文件的首页显示word图标,表示该PPT已包含配套word讲稿。双击word图标可打开word文档。
- 特殊限制:
部分文档作品中含有的国旗、国徽等图片,仅作为作品整体效果示例展示,禁止商用。设计者仅对作品中独创性部分享有著作权。
- 关 键 词:
- ISO632651989NATURALGASDETERMINATIONOFSULFURCOMPOUNDSPART5LINGENERCOMBUSTIONMETHOD 天然气 硫化物 测定 部分 林格聂尔

链接地址:http://www.mydoc123.com/p-1254685.html