EN 19694-3-2016 en Stationary source emissions - Determination of greenhouse gas (GHG) emissions in energy-intensive industries - Part 3 Cement industry《固定源排放量 能源密集型工业中温室气体排放的测定 第3.pdf

《EN 19694-3-2016 en Stationary source emissions - Determination of greenhouse gas (GHG) emissions in energy-intensive industries - Part 3 Cement industry《固定源排放量 能源密集型工业中温室气体排放的测定 第3.pdf》由会员分享，可在线阅读，更多相关《EN 19694-3-2016 en Stationary source emissions - Determination of greenhouse gas (GHG) emissions in energy-intensive industries - Part 3 Cement industry《固定源排放量 能源密集型工业中温室气体排放的测定 第3.pdf（80页珍藏版）》请在麦多课文档分享上搜索。

1、BS EN 19694-3:2016Stationary source emissions Determination of greenhousegas (GHG) emissions in energy-intensive industriesPart 3: Cement industryBSI Standards PublicationWB11885_BSI_StandardCovs_2013_AW.indd 1 15/05/2013 15:06BS EN 19694-3:2016 BRITISH STANDARDNational forewordThis British Standard

2、 is the UK implementation of EN 19694-3:2016.The UK participation in its preparation was entrusted to TechnicalCommittee EH/2/1, Stationary source emission.A list of organizations represented on this committee can beobtained on request to its secretary.This publication does not purport to include al

3、l the necessaryprovisions of a contract. Users are responsible for its correctapplication. The British Standards Institution 2016. Published by BSI StandardsLimited 2016ISBN 978 0 580 87114 6ICS 13.040.40Compliance with a British Standard cannot confer immunity fromlegal obligations.This British Sta

4、ndard was published under the authority of theStandards Policy and Strategy Committee on 31 July 2016.Amendments issued since publicationDate Text affectedBS EN 19694-3:2016EUROPEAN STANDARD NORME EUROPENNE EUROPISCHE NORM EN 19694-3 July 2016 ICS 13.040.40 English Version Stationary source emission

5、s - Determination of greenhouse gas (GHG) emissions in energy-intensive industries - Part 3: Cement industry missions de sources fixes - Dtermination des missions de gaz effet de serre (GES) dans les industries nergo-intensives - Partie 3: Industrie du ciment Emissionen aus stationren Quellen - Best

6、immung von Treibhausgasen (THG) aus energieintensiven Industrien - Teil 3: Zementindustrie This European Standard was approved by CEN on 5 May 2016. CEN members are bound to comply with the CEN/CENELEC Internal Regulations which stipulate the conditions for giving this European Standard the status o

7、f a national standard without any alteration. Up-to-date lists and bibliographical references concerning such national standards may be obtained on application to the CEN-CENELEC Management Centre or to any CEN member. This European Standard exists in three official versions (English, French, German

8、). A version in any other language made by translation under the responsibility of a CEN member into its own language and notified to the CEN-CENELEC Management Centre has the same status as the official versions. CEN members are the national standards bodies of Austria, Belgium, Bulgaria, Croatia,

9、Cyprus, Czech Republic, Denmark, Estonia, Finland, Former Yugoslav Republic of Macedonia, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland, Turkey andUnited

10、Kingdom. EUROPEAN COMMITTEE FOR STANDARDIZATION COMIT EUROPEN DE NORMALISATION EUROPISCHES KOMITEE FR NORMUNG CEN-CENELEC Management Centre: Avenue Marnix 17, B-1000 Brussels 2016 CEN All rights of exploitation in any form and by any means reserved worldwide for CEN national Members. Ref. No. EN 196

11、94-3:2016 EBS EN 19694-3:2016EN 19694-3:2016 (E) 2 Contents Page European foreword . 4 Introduction 5 1 Scope 9 2 Normative references 9 3 Terms and definitions . 9 4 Symbols and abbreviated terms . 12 5 Determination of GHGs based on the mass balance method 13 5.1 General . 13 5.2 Major GHG in ceme

12、nt 14 5.3 Determination based on mass balance 14 5.4 Determination by stack emission measurements 14 5.5 Gross and net emissions 14 6 System boundaries 21 6.1 General . 21 6.2 Operational boundaries . 21 6.3 Organizational boundaries . 22 7 Direct GHG emissions and their determination 25 7.1 General

13、 . 25 7.2 CO2from raw material calcinations . 28 7.3 Reporting of CO2emissions from raw material calcination based on clinker output: summary of IPCC and CSI recommendations and default emission factor for clinker . 37 7.4 Determining the FD calcination rate . 38 7.5 Direct determination of the CO2e

14、mission factor of FD from analysis of CO2content . 39 7.6 Cement specific issues for fuels 39 7.7 GHG from fuels for kilns . 41 7.8 GHG from non-kiln fuels 41 7.9 GHG from the combustion of wastewater 42 7.10 Non-CO2GHG emissions from the cement industry . 42 8 Energy indirect and other indirect GHG

15、 emissions and their determination 43 8.1 General . 43 8.2 CO2from external electricity production 43 8.3 CO2from bought clinker 44 9 Baselines, acquisitions and disinvestments . 44 10 Reporting 45 10.1 General . 45 10.2 Corporate environmental reporting . 45 10.3 Reporting periods 46 10.4 Performan

16、ce indicators . 47 11 Uncertainty of GHG inventories 53 11.1 Introduction to uncertainty assessment . 53 11.2 Uncertainty of activity data 56 11.3 Uncertainties of fuel and material parameters . 56 BS EN 19694-3:2016EN 19694-3:2016 (E) 3 11.4 Uncertainties of continuous stack emission measurements 5

17、7 11.5 Evaluation of the overall uncertainty of a GHG inventory . 58 11.6 Application of default values instead of analysing results 58 12 Considerations for applying this standard (verification procedure) 59 Annex A (informative) Findings from the field tests (analytical interferences). 61 Annex B

18、(informative) Emission factors 65 Annex C (informative) Uncertainty of activity data . 67 Annex D (informative) Overview on terms in a cement plant 73 Bibliography . 75 BS EN 19694-3:2016EN 19694-3:2016 (E) 4 European foreword This document (EN 19694-3:2016) has been prepared by Technical Committee

19、CEN/TC 264 “Air quality”, the secretariat of which is held by DIN. This European Standard shall be given the status of a national standard, either by publication of an identical text or by endorsement, at the latest by January 2017, and conflicting national standards shall be withdrawn at the latest

20、 by January 2017. Attention is drawn to the possibility that some of the elements of this document may be the subject of patent rights. CEN and/or CENELEC shall not be held responsible for identifying any or all such patent rights. This document has been prepared under a mandate M/478 given to CEN b

21、y the European Commission and the European Free Trade Association. EN 19694, Stationary source emissions Determination of greenhouse gas (GHG) emissions in energy-intensive industries is a series of standards that consists of the following parts: Part 1: General aspects Part 2: Iron and steel indust

22、ry Part 3: Cement industry Part 4: Aluminium industry Part 5: Lime industry Part 6: Ferroalloy industry According to the CEN/CENELEC Internal Regulations, the national standards organizations of the following countries are bound to implement this European Standard: Austria, Belgium, Bulgaria, Croati

23、a, Cyprus, Czech Republic, Denmark, Estonia, Finland, Former Yugoslav Republic of Macedonia, France, Germany, Greece, Hungary, Iceland, Ireland, Italy, Latvia, Lithuania, Luxembourg, Malta, Netherlands, Norway, Poland, Portugal, Romania, Slovakia, Slovenia, Spain, Sweden, Switzerland, Turkey and the

24、 United Kingdom. BS EN 19694-3:2016EN 19694-3:2016 (E) 5 Introduction This European Standard for the cement industry has been based on the WBCSD/CSI and WRI: “CO2and Energy Accounting and Reporting Standard for the Cement Industry” 1. Overview of cement manufacturing process Cement manufacture inclu

25、des three main process steps (see Figure 1): a) preparing of raw materials and fuels; b) producing clinker, an intermediate, through pyro-processing of raw materials; c) grinding and blending clinker with other products (“mineral components”) to make cement. There are two main sources of direct CO2e

26、missions in the production process: calcination of raw materials in the pyro-processing stage, and combustion of kiln fuels. These two sources are described in more detail below. Other CO2sources include direct GHG emissions from non-kiln fuels (e.g. dryers for cement constituents products, room hea

27、ting, on-site transports and on-site power generation), and indirect GHG emissions from, e.g. external power production and transports. Non-CO2greenhouse gases covered by the Kyoto Protocol1, apart from carbon monoxide (CO) methane (CH4) and nitrous oxide (N2O), are not relevant in the cement contex

28、t, in the sense that direct GHG emissions of these gases are negligible. Figure 1 Process steps in cement manufacture (source: Ellis 2000, based on Ruth et al. 2000) 1Methane (CH4), nitrous oxide (N2O), sulfur hexafluoride (SF6), partly halogenated fluorohydrogencarbons (HFC) and perfluorated hydroc

29、arbons (PFC) BS EN 19694-3:2016EN 19694-3:2016 (E) 6 Table 1 Overview of input places of materials Raw meal Input place Raw materials from natural resources Raw mill Alternative raw materials Raw mill Raw material flows for clinker production Input place Raw meal Kiln feed Fuel ashes Burner or preca

30、lciner or fuel dryer Additional raw materials not part of the kiln feed Kiln inlet Fuels flows for clinker and cement production Input place Fossil fuels Burner or precalciner or fuel dryer or raw material dryer Alternative fuels Burner or precalciner or fuel dryer or raw material dryer Alternative

31、fossil fuels Burner or precalciner or fuel dryer or raw material dryer Mixed fuels Burner or precalciner or fuel dryer or raw material dryer Biomass fuels Burner or precalciner or fuel dryer or raw material dryer Cement kiln dust Output place Dust return Preheater Filter dust Precipitator / filter B

32、y pass dust Bypass filter Cement constituents based products Output place Clinker Kiln (cooler) Cement Cement mill Blast furnace slag Cement mill or grinding station Fly ash Cement mill or grinding station Gypsum Cement mill or grinding station Cooler dust Cooler, is normally added to the clinker fl

33、ow to the clinker silo Cement kiln dust Preheater or precipitator or filter or bypass filter Limestone Cement mill or grinding station Burnt shale Cement mill or grinding station Pozzolana Cement mill or grinding station Silica fume Cement mill or grinding station BS EN 19694-3:2016EN 19694-3:2016 (

34、E) 7 CO2from calcination of raw materials In the clinker production process, CO2is released due to the chemical decomposition of calcium, magnesium and other carbonates (e.g. from limestone) into lime: CaCO3+ heat CaO + CO2MgCO3+ heat MgO + CO2This process is called “calcining“ or “calcination“. It

35、results in direct CO2emissions through the kiln stack. When considering CO2emissions due to calcination, two components may be distinguished: CO2from raw materials actually used for clinker production, these raw materials are fully calcined in the clinker production process; CO2from raw materials le

36、aving the kiln system as partly calcined cement kiln dust (CKD), or as normally fully calcined bypass dust. CO2from actual clinker production is proportional to the lime content of the clinker,2, which in turn varies little in time or between different cement plants. As a result, the CO2emission fac

37、tor per tonne of clinker is fairly stable with a default value in this standard of 525 kg CO2/t clinker (IPCC default: 510 kg CO2/t clinker, CSI default: 525 kg CO2/t clinker 19). The amount of kiln dust leaving the kiln system varies greatly with kiln types and cement quality standards, ranging fro

38、m practically zero to over one hundred kilograms per tonne of clinker. The associated emissions are likely to be relevant in some countries or installations. CO2emissions from calcination of raw materials may be calculated by two methods which are in principle equivalent: Either based on the amount

39、and chemical composition of the products (clinker plus dust leaving the kiln system, output methods B1 and B2), or based on the amount and composition of the raw materials entering the kiln (input methods A1 and A2). See 7.2.1, 7.2.2 for details. CO2from organic carbon in raw materials The raw mater

40、ials used for clinker production usually contain a small fraction of organic carbon, which may be expressed as total organic carbon (TOC) content. Organic carbon in the raw meal is converted to CO2during pyro-processing. The contribution of this component to the overall CO2emissions of a cement plan

41、t is typically very small (about 1 % or less). The organic carbon contents of raw materials may, however, vary substantially between locations and between the types of materials used. For example, the resulting emissions may be relevant if a cement company organization (used in this standard) consum

42、es large quantities of certain types of fly ash or shale as raw materials entering the kiln. CO2from fuels for kiln operation The cement industry traditionally uses various fossil fuels to operate cement kilns, including coal, petroleum coke, fuel oil, and natural gas. Fuels derived from waste mater

43、ials have become important substitutes for traditional fossil fuels. These alternative fuels (AF) include fossil fuel-derived fractions such as, e.g. waste oil and plastics, as well as biomass-derived fractions such as waste wood and dewatered sludge from wastewater treatment. Furthermore fuels are

44、increasingly used which contain both fossil and biogenic carbon (mixed fuels), like e.g. (pre-treated) municipal and (pre-treated) industrial wastes (containing plastics, textiles, paper etc.) or waste tyres (containing natural and synthetic rubber). 2A second, but much smaller factor is the CaO and

45、 MgO content of the raw materials and additives used. BS EN 19694-3:2016EN 19694-3:2016 (E) 8 Both traditional fossil and alternative fuels result in direct CO2emissions through the kiln stack. However, biomass and bioliquids are considered “climate change-neutral“ in accordance with IPCC definition

46、s. Use of alternative (biomass- or fossil-derived) fuels may, in addition, lead to important emission reductions elsewhere, for instance from waste incineration plants or landfills. Mineral components (MIC) are natural and artificial materials with latent hydraulic properties. Examples of MIC includ

47、e natural pozzolana, blast furnace slag, and fly ash. In addition, gypsum is within this standard labelled as MIC. MICs are added to clinker to produce blended cement. In some instances, pure MICs are directly added to the concrete by the ready-mix or construction company. Use of MICs leads to an eq

48、uivalent reduction of direct CO2emissions associated with clinker production, both from calcination and fuel combustion. Artificial MICs are waste materials from other production processes such as, e.g. steel and coal-fired power production. Related GHG emissions are monitored and reported by the co

49、rresponding industry sector. Utilization of these MICs for clinker or cement substitution does not entail additional GHG emissions at the production site. Consequently, these indirect GHG emissions shall not be included in the cement production inventory. The basic mass balance methods used in this standard are compatible with the 2006 IPCC Guidelines for National Greenhouse Gas Inventories issued by the Intergovernmental Panel on Climate Change (IPCC) 4, and with the revised WRI / WBCSD Greenhouse Gas Protocol 9. Default emission factors