关于确定危险废物焚烧炉防护距离的建议

整理文档很辛苦,赏杯茶钱您下走!

免费阅读已结束,点击下载阅读编辑剩下 ...

阅读已结束,您可以下载文档离线阅读编辑

资源描述

2018-03-031972—。121.2500142.250014。。X327B1008-021X201807-0174-04SuggestionsforDeterminingtheProtectionDistanceofHazardousWasteIncineratorsZhangQiang1ZhangYixin21.ShandongChemicalIndustryResearchInstituteofQingdaoUniversityofScienceandTechnologyJinan250014China2.HighSchoolAttachedtoShandongNormalUniversityJinan250014ChinaAbstractTheenvironmentalprotectiondistancehealthprotectiondistanceofhazardouswasteincineratorhasnotyetbeenclearlydefined.TakinganincineratorofanenterpriseinShandongProvinceasanexamplethispaperputsforwardthesuggestionofdeterminingtheenvironmentalprotectiondistancehealthprotectiondistanceofhazardouswasteincineratorthroughthepredictionandcalculationofenvironmentalriskaccidents.Keywordshazardouswasteincineratorhealthprotectiondistanceenvironmentalprotectiondistancedioxin。、、、、、。1。。、、2-3。《》HJ/T176-2005、800m。201267《<》HJ/T176-2005》201233、、。11987。2《》200882、。。《》GB/T3840-91。201233200882300m。。《》200882。。《<、>GB18599-20013》201336“、、、、、。”200882。。1、、、1800kg/h。+++++35m。。·471·SHANDONGCHEMICALINDUSTRY201847DOI:10.19319/j.cnki.issn.1008-021x.2018.07.07371.1。。。420ngTEQ/m3100m32000ngTEQ。1。1Table1Summaryofriskaccidentonesource100m31100℃2000ngTEQ0.5min66.7ngTEQ/s3.33m3/s0.2m6m0.2、1.0、1.5、2.0、2.3、3.0m/sD、E、F《》HJ/T2.2-93。12m3。。2008824pgTEQ/kg10%0.4pgTEQ/kg·d。50kg20pgTEQ/d。1。D、3m/s2。2700m。2Table2Maximumoverstandardrangelistofriskaccidentone/m/pgTEQ/m3/pgTEQ/d/%00001000002000003000004000.00280.0340.175001.016812.20261.016001.813321.760108.807000.41975.03625.188000.04430.5322.669000.00360.0430.2210000.00030.0040.02D、3m/s。20pgTEQ/d。100m3。3。3Table3Theenvironmentalprotectiondistancehealthprotectiondistanceofhazardouswasteincineratorlistrefertoriskaccidentone/m3/m/m3/m/m3/m1030080600150800204009060016080030500100700170800405001107001808005050012070019080060600130700200900706001407001.2。420ngTEQ/m3。·571·1800kg/h10800m3/h20ngTEQ/m380℃35m1.2m。Screen3Model。12m320pgTEQ/d。4。4600m。4Table4Maximumoverstandardrangelistofriskaccidenttwo/m/pgTEQ/m3/pgTEQ/d*/%/m/pgTEQ/m3/pgTEQ/d*/%00006001.56418.7793.841000.1041.256.247001.62519.5097.502001.27715.3276.628001.62019.4497.203001.82321.88109.389001.55018.6093.004001.75421.05105.2410001.45117.4187.065001.68720.24101.22*20pgTEQ/d。1800kg/h。5。《》GB18484-2001≤300kg/h25m300~2000kg/h35m2000~2500kg/h45m≥2500kg/h50m。5Table5Theenvironmentalprotectiondistancehealthprotectiondistanceofhazardouswasteincineratorlistrefertoriskaccidenttwo/kg/h/m3/h/m/ng/s/m1006000.83.3325300m*20012000.86.6725300m*25015000.88.3325300m*30018000.810.0025300m*40024001.213.3335300m*50030001.216.6735300m*60036001.220.0035300m*70042001.223.3335300m*80048001.226.6735300m*90054001.230.0035300m*100060001.233.3335300m*110066001.236.6735300m*120072001.240.0035300m*130078001.243.3335300m*140084001.246.6735300m*150090001.250.0035400m160096001.253.3335400m1700102001.256.6735400m1800108001.260.0035600m1900114001.263.3335600m2000120001.566.6745300m*2100126001.570.0045300m*2200132001.573.3345300m*·671·SHANDONGCHEMICALINDUSTRY20184775/kg/h/m3/h/m/ng/s/m2300138001.576.6745300m*2400144001.58045400m250015000283.3350300m*260015600286.6750300m*27001620029050300m*280016800293.3350300m*290017400296.6750500m300018000210050500m“*”。200882300m“*”300m。2、700m600m。。35、、。1.J.200821557.2.J.200917356-58.3.J.20164319146-147.4.C//.2008245-248..J.2018477174-177.櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀櫀16915HongJChaudhryGBrissonJGetal.Analysisofoxy-fuelcombustionpowercycleutilizingapressurizedcoalcombustorJ.Energy20093491332-1340.16RinkerEBAndSSASandallOC.AbsorptionofcarbondioxideintoaqueousblendsofdiethanolamineandmethyldiethanolamineJ.Industrial&EngineeringChemistryResearch200639114346-4356.17AboudheirATontiwachwuthikulPChakmaAetal.KineticsofreactiveabsorptionofcarbondioxideinhighCO2-loadedconcentratedaqueousmonoethanolaminesolutionsJ.ChemicalEngineeringScience200358235195-5210.18MoullecYLKannicheM.ScreeningofflowsheetmodificationsforanefficientmonoethanolamineMEAbasedpost-combustionCO2captureJ.InternationalJournalofGreenhouseGasControl201154727-740.19LeonardGMogadorBCBelletanteSetal.Dynamicmodellingandcontrolofapilotplantforpost-combustionCO2captureJ.ComputerAidedChemicalEngineering20133212451-456.20RaynalLBouillonPAGomezAetal.FromMEAtodemixingsolventsandfuturestepsaroadmapforloweringthecostofpost-combustioncarboncaptureJ.ChemicalEngineeringJournal20111713742-752.21SakwattanapongRAdisornAroonwilasAVeawabA.BehaviorofreboilerheatdutyforCO2captureplantsusingregenerablesingleandblendedalkanolaminesJ.Industrial&EngineeringChemistryResearch200544124465-4473..CO2J.2018477165-169177.櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌櫌17323.CN102951769BP.2013-12-25.24./J.201615196-99.25.PO_MTBED.2016.26.J.20174115-7.27.CHPHPPOJ.201241201-204.28.BASF-DowHPPOJ.2011958-23.29.Degussa-UhdeHPPOJ.20097215-2230.30.HPPOJ.201126140-43.31.FentonJ.201616827-30..J.2018477170-173177.·771·://://ppt.ixueshu.com-------------------------------------------------------------------------------

1 / 5
下载文档,编辑使用

©2015-2020 m.777doc.com 三七文档.

备案号:鲁ICP备2024069028号-1 客服联系 QQ:2149211541

×
保存成功