ASTM D6559-2000a(2010) 2500 Standard Test Method for Determination of Thermogravimetric (TGA) Air Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的热重(TGA)气体反应性的标准试验方法.pdf
《ASTM D6559-2000a(2010) 2500 Standard Test Method for Determination of Thermogravimetric (TGA) Air Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的热重(TGA)气体反应性的标准试验方法.pdf》由会员分享,可在线阅读,更多相关《ASTM D6559-2000a(2010) 2500 Standard Test Method for Determination of Thermogravimetric (TGA) Air Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的热重(TGA)气体反应性的标准试验方法.pdf(5页珍藏版)》请在麦多课文档分享上搜索。
1、Designation: D6559 00a (Reapproved 2010)Standard Test Method forDetermination of Thermogravimetric (TGA) Air Reactivity ofBaked Carbon Anodes and Cathode Blocks1This standard is issued under the fixed designation D6559; the number immediately following the designation indicates the year oforiginal a
2、doption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. Asuperscript epsilon () indicates an editorial change since the last revision or reapproval.1. Scope1.1 This test method covers the thermogravimetric (TGA)determination of a
3、ir reactivity and dusting of shaped carbonanodes and cathode blocks used in the aluminum reductionindustry. The apparatus selection covers a significant variety oftypes with various thermal conditions, sample size capability,materials of construction, and procedures for determining themass loss and
4、subsequent rate of reaction. This test methodstandardizes the variables of sample dimensions, reactiontemperature, gas velocity over the exposed surfaces, andreaction time such that results obtained on different apparatusesare correlatable.1.2 The values stated in SI units are to be regarded asstand
5、ard. No other units of measurement are included in thisstandard.1.3 This standard does not purport to address all of thesafety concerns, if any, associated with its use. It is theresponsibility of the user of this standard to establish appro-priate safety and health practices and determine the appli
6、ca-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D6353 Guide for Sampling Plan and Core Sampling forPrebaked Anodes Used in Aluminum ProductionD6354 Guide for Sampling Plan and Core Sampling ofCarbon Cathode Blocks Used in Aluminum ProductionE691 Practice f
7、or Conducting an Interlaboratory Study toDetermine the Precision of a Test Method3. Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 dusting, nthe quantity of carbon that falls off thecarbon artifact while in the reaction chamber and is collected inthe container at the bottom of t
8、he reaction chamber.3.1.2 final air reactivity, nthe mass loss of the carbonartifact during the final 30 min of exposure to air in the reactionchamber divided by the initial geometric (right cylindrical)exposed surface area of the sample, expressed as mg/cm2-h.3.1.3 initial air reactivity, nthe mass
9、 loss of the carbonartifact during the first 30 min of exposure to air in the reactionchamber divided by the initial geometric (right cylindrical)exposed surface area of the sample, expressed as mg/cm2-h.3.1.4 total air reactivity, nthe total mass loss of thecarbon artifact (including dusting) durin
10、g the total time that thesample is exposed to air (180 min) in the reaction chamberdivided by the initial geometric (right cylindrical) exposedsurface area of the sample, expressed as mg/cm2-h.4. Summary of Test Method4.1 Initial, final, and total air reactivity and dusting aredetermined by passing
11、air at flow rates, giving a standardvelocity of reactant gas around cylindrically shaped carbonartifacts under nearly isothermal conditions for a specifiedlength of time. The reactivity is determined by continuouslymonitoring the sample mass loss. The dusting term is deter-mined by collecting and de
12、termining the mass of carbonparticles that fall off the sample during reaction.5. Significance and Use5.1 The air reactivity rates are used to quantify the tendencyof a carbon artifact to react with air. Carbon consumed by thisunwanted side reaction is unavailable for the primary reactionsof reducin
13、g alumina to the primary metal.Air reactivity dustingrate is used by some companies to quantify the tendency of thecoke aggregate or binder coke of a carbon artifact to selectivelyreact with these gases. Preferential attack of the binder coke orcoke aggregate of a carbon artifact by these gases caus
14、es somecarbon to fall off or dust, making the carbon unavailable for the1This test method is under the jurisdiction of ASTM Committee D02 onPetroleum Products and Lubricants and is the direct responsibility of SubcommitteeD02.05 on Properties of Fuels, Petroleum Coke and Carbon Material.Current edit
15、ion approved May 1, 2010. Published May 2010. Originallyapproved in 2000. Last previous edition approved in 2005 as D655900a (2005).DOI: 10.1520/D6559-00AR10.2For referenced ASTM standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of A
16、STMStandards volume information, refer to the standards Document Summary page onthe ASTM website.1Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959, United States.primary reaction of reducing alumina and, more importantly,reducing the efficiency of th
17、e aluminum reduction cell.5.2 Comparison of air reactivity and dusting rates is usefulin selecting raw materials for the manufacture of commercialanodes for specific smelting technologies in the aluminumreduction industry.5.3 Air reactivity rates are used for evaluating effectivenessand beneficiatio
18、n processes or for research purposes.6. Apparatus6.1 The apparatus to be used should be as simple as possibleand be commensurate with what is to be achieved, the principalcriteria being that the reaction rate is to be determined underisothermal conditions and unaffected by physical and chemicalprope
19、rties inherent to the apparatus (such as gas diffusionpatterns, gas temperature, exposed sample surface area, and soforth). A typical apparatus that has been found to be suitable isillustrated in Fig. 1.6.1.1 Furnace and Controller, capable of maintaining con-stant temperature within 62C in the 100-
20、mm region centeredon the specimen. The example apparatus of Fig. 1 employs athree zone heating element and associated controls to accom-plish this, but other methods such as tapered windings or longlinear heaters are also suitable. The control thermocouple is agrounded type and shall be located with
21、in the reaction chambernear the surface of the test sample to allow the furnacecontroller to adjust to the exothermic reaction that occursduring the air reactivity test. The control thermocouple shall bepositioned 4 6 1 mm from the side sample surface andcentered vertically within 5 mm of the center
22、. The furnace shallbe large enough to accept the reaction chamber.6.1.2 Reaction Chamber, consisting of a vertical tube con-structed of a material capable of withstanding the temperatureof the reaction with sufficient inside diameter (ID) to accept thesample and sample holder while not affecting the
23、 gas flow toand from the sample (100 6 25-mm ID is recommended). Thereaction chamber is to be constructed with a dust collection cupat the bottom, which is removable and capable of capturing allthe dust that falls off the sample during the test. The mostcommon materials of construction are quartz an
24、d Inconel.6.1.3 Sample Holders, capable of supporting the sample inthe reaction chamber for the duration of the test and should becapable of being reusable. The sample holder shall not changein mass during the test, affect the diffusion pattern of the gasesto or from the sample, limit the gas access
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