ASTM E777-17a Standard Test Method for Carbon and Hydrogen in the Analysis Sample of Refuse-Derived Fuel.pdf
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1、Designation: E777 17aStandard Test Method forCarbon and Hydrogen in the Analysis Sample of Refuse-Derived Fuel1This standard is issued under the fixed designation E777; the number immediately following the designation indicates the year oforiginal adoption or, in the case of revision, the year of la
2、st 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 is for the determination of total carbonand hydrogen in a sample of refuse-derived fuel (RDF). Bothcarb
3、on and hydrogen are determined in one analysis. This testmethod yields the total percentages of carbon and hydrogen inRDF as analyzed and the results include not only carbon andhydrogen in the organic matter, but also the carbon present inmineral carbonates and the hydrogen present in the freemoistu
4、re accompanying the analysis sample as well as hydro-gen present as water of hydration.NOTE 1It is recognized that certain technical applications of the dataderived from this test procedure may justify additional corrections. Thesecorrections could involve compensation for the carbon present ascarbo
5、nates, the hydrogen of free moisture accompanying the analysissample, and the calculated hydrogen present as water of hydration.1.2 This test method may be applicable to any wastematerial from which a laboratory analysis sample can beprepared.1.3 The values stated in SI units are to be regarded asst
6、andard. No other units of measurement are included in thisstandard.1.4 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, health, and environmental practices and
7、deter-mine the applicability of regulatory limitations prior to use.For specific precautionary statements, see Section 8.1.5 This international standard was developed in accor-dance with internationally recognized principles on standard-ization established in the Decision on Principles for theDevelo
8、pment of International Standards, Guides and Recom-mendations issued by the World Trade Organization TechnicalBarriers to Trade (TBT) Committee.2. Referenced Documents2.1 ASTM Standards:2D1193 Specification for Reagent WaterD5681 Terminology for Waste and Waste ManagementE790 Test Method for Residua
9、l Moisture in Refuse-DerivedFuel Analysis SamplesE791 Test Method for Calculating Refuse-Derived FuelAnalysis Data from As-Determined to Different BasesE829 Practice for Preparing Refuse-Derived Fuel (RDF)Laboratory Samples for Analysis3. Terminology3.1 For definitions of terms used in this test met
10、hod, refer toTerminology D5681.4. Summary of Test Method4.1 The determination is made by burning the sample toconvert carbon to carbon dioxide and hydrogen to water. Thecombustion is carried out using high-purity oxygen that hasbeen passed through a purifying train. The carbon dioxide andwater are r
11、ecovered in an absorption train. Combustion tubepacking is used to remove interfering substances. This testmethod gives the total percentage of carbon and hydrogen inthe RDF as analyzed, including the carbon in carbonates andthe hydrogen in water.5. Significance and Use5.1 This standard is intended
12、to provide a method fordetermining the weight percent of carbon and hydrogen in anRDF analysis sample.5.2 Carbon and hydrogen are components of RDF and,when determined, can be used for calculating RDF combustioncharacteristics.6. Apparatus6.1 Oxygen Purifying TrainHigh-purity oxygen is passedthrough
13、 water and carbon dioxide absorbers prior to use for1This test method is under the jurisdiction of ASTM Committee D34 on WasteManagement and is the direct responsibility of Subcommittee D34.03 on Treatment,Recovery and Reuse.Current edition approved Dec. 1, 2017. Published December 2017. Originallya
14、pproved in 1987. Last previous edition approved in 2017 as E777 17. DOI:10.1520/E0777-17A.2For referenced ASTM 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 Sum
15、mary page onthe ASTM website.Copyright ASTM International, 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959. United StatesThis international standard was developed in accordance with internationally recognized principles on standardization established in the Decision on Principle
16、s for theDevelopment of International Standards, Guides and Recommendations issued by the World Trade Organization Technical Barriers to Trade (TBT) Committee.1combustion. The oxygen purifying train consists of the follow-ing three components in order of gas passage (see Fig. 1):6.1.1 First Water Ab
17、sorberA container constructed suchthat oxygen must pass through a column of water-removingreagent. The container shall have a capacity for at least 45 cm3of solid reagent, and the minimum gas distance traveledthrough the reagent shall be at least 80 mm.6.1.2 Carbon Dioxide AbsorberIf solid reagents
18、are usedfor carbon dioxide absorption, the container shall be asdescribed in 6.1.1. If a solution is used, the container shall bea Vanier bulb. It shall provide a column of reagent adequate toremove carbon dioxide below the testing laboratorys analyticreporting limit.6.1.3 Second Water AbsorberSame
19、as specified in 6.1.1.6.2 Flow Meter, used to permit volumetric measurement ofthe rate of flow of oxygen during the determination. It shall besuitable for measuring flow rates within the range from 50 to100 mL/min. The use of a double-stage pressure-reducingregulator with gage and needle valve is re
20、commended to permiteasy and accurate adjustment to the rate of flow.6.3 Combustion Unit, consisting of three electrically heatedfurnace sections, individually controlled, which may bemounted on rails for easy movement. The upper part of eachfurnace may be hinged so that it can be opened for inspecti
21、onof the combustion tube. The three furnace sections shall be asfollows (see Fig. 1):6.3.1 Furnace Section 1Furnace 1 is nearest the oxygeninlet of the combustion tube, approximately 130 mm long andused to heat the inlet of the combustion tube and the sample. Itshall be capable of rapidly attaining
22、an operating temperatureof 875 6 25 C.NOTE 2Combustion tube temperature shall be measured by means ofa thermocouple placed immediately adjacent to the tube near the center ofthe appropriate tube section.6.3.2 Furnace Section 2Furnace 2 shall be approximately330 mm in length and used to heat that por
23、tion of the tube filledwith cupric oxide. The operating temperature shall be 850 620 C (see Note 2).6.3.3 Furnace Section 3Furnace 3 shall be approximately230 mm long, and used to heat that portion of the tube filledwith lead chromate or silver. The operating temperature shallbe 500 6 50 C.6.3.4 Com
24、bustion Tube, made of fused quartz, or high-silicaglass and having a nominal inside diameter which may varywithin the limits of 19 to 22 mm and a minimum total lengthof 970 mm. The exit shall be tapered to provide a tubulatedsection for connection to the absorption train. The tubulatedsection shall
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