ASTM D6558-2000a(2005) Standard Test Method for Determination of TGA CO2 Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的TGA CO2反应性的标准试验方法》.pdf
《ASTM D6558-2000a(2005) Standard Test Method for Determination of TGA CO2 Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的TGA CO2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 D6558-2000a(2005) Standard Test Method for Determination of TGA CO2 Reactivity of Baked Carbon Anodes and Cathode Blocks《测定碳阳极和阴极块的TGA CO2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: D 6558 00a (Reapproved 2005)An American National StandardStandard Test Method forDetermination of TGA CO2Reactivity of Baked CarbonAnodes and Cathode Blocks1This standard is issued under the fixed designation D 6558; the number immediately following the designation indicates the year of
2、original adoption or, in the case of revision, the year of last revision. A number in parentheses indicates the year of last reapproval. Asuperscript epsilon (e) indicates an editorial change since the last revision or reapproval.1. Scope1.1 This test method covers the thermogravimetric (TGA)determi
3、nation of CO2reactivity 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
4、 loss and 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 regard
5、ed asstandard. 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
6、 the applica-bility of regulatory limitations prior to use.2. Referenced Documents2.1 ASTM Standards:2D 6353 Guide for Sampling Plan and Core Sampling ofPrebaked Anodes Used in Aluminum ProductionD 6354 Guide for Sampling Plan and Core Sampling ofCarbon Cathode Blocks Used in Aluminum ProductionE 69
7、1 Practice for Conducting an Interlaboratory Study toDetermine the Precision of a Test Method3. Terminology3.1 Definitions of Terms Specific to This Standard:3.1.1 dusting, nthat quantity of carbon that falls off thecarbon artifact while in the reaction chamber and is collected inthe container at th
8、e bottom of the reaction chamber.3.1.2 final CO2reactivity, nthe mass loss of the carbonartifact during the final 30 min of exposure to CO2in thereaction chamber divided by the initial geometric (right cylin-drical) exposed surface area of the sample, expressed asmg/cm2-h.3.1.3 initial CO2reactivity
9、, nthe mass loss of the carbonartifact during the first 30 min of exposure to CO2in thereaction chamber divided by the initial geometric (right cylin-drical) exposed surface area of the sample, expressed asmg/cm2-h.3.1.4 total CO2reactivity, nthe total mass loss of thecarbon artifact (including dust
10、ing) during the total time that thesample is exposed to CO2(420 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 CO2reactivity and dusting aredetermined by
11、passing carbon dioxide gas at flow rates givinga standard velocity of reactant gas around cylindrically shapedcarbon artifacts under isothermal conditions for a specifiedlength of time. The reactivity is determined by continuouslymonitoring the sample mass loss. The dusting term is deter-mined by co
12、llecting and determining the mass of carbonparticles that fall off the sample during reaction.5. Significance and Use5.1 The CO2reactivity rates are used to quantify thetendency of a carbon artifact to react with carbon dioxide.Carbon consumed by these unwanted side reactions is unavail-able for the
13、 primary reactions of reducing alumina to theprimary metal. CO2dusting rates are used to quantify thetendency of the coke aggregate or binder coke of a carbonartifact to selectively react with these gases. Preferential attack1This test method is under the jurisdiction of ASTM Committee D02 onPetrole
14、um Products and Lubricants and is the direct responsibility of SubcommitteeD02.05 on Properties of Fuels, Petroleum Coke and Carbon Material.Current edition approved May 1, 2005. Published June 2005. Originallyapproved in 2000. Last previous edition approved in 2000 as D 655800a.2For referenced ASTM
15、 standards, visit the ASTM website, www.astm.org, orcontact ASTM Customer Service at serviceastm.org. For Annual Book of ASTMStandards volume information, refer to the standards Document Summary page onthe ASTM website.1Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohoc
16、ken, PA 19428-2959, United States.of the binder coke or coke aggregate of a carbon artifact bythese gases causes some carbon to fall off or dust, making thecarbon unavailable for the primary reaction of reducing alu-mina and, more importantly, reducing the efficiency of thealuminum reduction cell.5.
17、2 Comparison of CO2reactivity and dusting rates is usefulin selecting raw materials for the manufacture of commercialanodes for specific smelting technologies in the aluminumreduction industry.5.3 CO2reactivity rates are used for evaluating effectivenessand beneficiation processes or for research pu
18、rposes.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 chemicalproperties inherent to the apparatu
19、s (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-mm region centeredon the spec
20、imen. 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 within the reaction chambernear t
21、he surface of the test sample to allow the furnacecontroller to adjust to exothermic reactions, which occurduring air reactivity tests, if the furnace is also used for airreactivity testing. The control thermocouple shall be positioned4 6 1 mm from the side sample surface and centered verticallywith
22、in 5 mm of the center. The furnace shall be large enoughto accept the reaction chamber.6.1.1.1 Reaction Chamber, consisting of a vertical tubeconstructed of a material capable of withstanding the tempera-ture of the reaction (960 6 2C) with sufficient inside diameter(ID) to accept the sample and sam
23、ple holder while not affectingthe gas flow to and from the sample (100 6 25-mm ID isrecommended). The reaction chamber is to be constructed witha dust collection cup at the bottom that is removable andcapable of capturing all the dust that falls off the sample duringthe test. The most common materia
24、ls of construction are quartzand Inconel.6.1.1.2 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
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