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Process Data set: Toluene; production mix, at plant (en) en

Key Data Set Information
Location EU-28
Geographical representativeness description EU27 including Norway
Reference year 2008
Name
Base name ; Mix and location types
Toluene; production mix, at plant
Synonyms Methylbenzene
Classification
Class name : Hierarchy level
  • ILCD: Materials production / Plastics
General comment on data set Disclaimer: The LCI and LCIA results of this dataset can vary from the published Eco-profile on PlasticsEurope website due to the conversion of the original LCI to an ILCD compliant LCI, and some updates of characterization factors used in the Eco-profile since the time of the publication. This was done in agreement with PlasticsEurope.
Copyright Yes
Time representativeness
Data set valid until 2013
Time representativeness description time to which data mainly refer: 2008 - 2010
Technological representativeness
Technology description including background system "Toluene is commercially produced based on two different feedstocks: - Pyrolysis gasoline, a side product of thermal cracking (steam cracking) of hydrocarbons (e.g. naphtha, gas oil, ethane, propane, butanes, natural gas liquids) - Reformate, a product of catalytic reforming of naphtha Additionally, the three aromatics BTX can be chemically transferred into each other by means of transalkylation and disproportionation reactions (for example toluene to benzene and xylenes). In Europe (EU27) benzene is mainly produced via pyrolysis gasoline (30 %) and reformate (70 %). Raw pyrolysis gasoline has to be hydrotreated. The further processing steps of hydrotreated pyrolysis gasoline and reformate are basically identical. The feedstock (either hydrotreated pyrolysis gasoline or reformate) is fractionated in a first distillation column into a benzene/toluene cut, which contains also the nonaromatic compounds, and into the higher boiling xylenes (including ethylbenzene and styrene) and higher aromatics fraction. Benzene and toluene are separated from the nonaromatics (raffinate) by solvent extraction (liquid-liquid extraction). In a transalkylation/disproportionation unit, overhead toluene can be converted into additional xylenes. For transalkylation, higher aromatics (e.g. trimethylbenzenes) are co-fed with toluene to produce only xylenes. During disproportionation, two toluene molecules react to form one molecule of benzene and xylenes, respectively. Toluene can also be fed to a hydrodealkylation unit to produce additional benzene and methane. The xylenes and higher aromatics obtained at the bottom of the feed splitter column together with the xylenes produced in the transalkylation/disproportionation unit are charged to a xylene column. This fractionation unit is designed to either completely separate the xylenes from higher aromatics or to recover also a part of o-xylene in the bottoms. In the latter case, o-xylene can be obtained as product after another distillation step. Higher aromatics (C9+) are either used in toluene transalkylation or blended into the gasoline pool. The xylenes from the top of the xylene column are fed to the so-called xylene loop, consisting of a p-xylene extraction unit and a xylene isomerisation unit. In the first unit high purity p-xylene is extracted from the equilibrium xylene mixture either by crystallization or by adsorptive separation. The remaining xylene mixture (containing also ethylbenzene and styrene) is fed to an isomerisation unit where a near-equilibrium distribution of xylene isomers is re-established, meaning that new p-xylene is formed from the remaining o- and m-xylenes. The catalyst used here also isomerizes ethylbenzene selectively to xylene isomers in their equilibrium ratio. Hydrogen is added to the isomerisation unit to prevent hydrogenolysis of the aromatics on the metal sites. After separation from light by-products (light ends (methane and hydrogen), benzene, toluene) through fractionation and from unsaturated components the mixed xylenes (and by-product C9+-aromatics) are recycled to the xylene column."
LCI method and allocation
Type of data set LCI result
LCI Method Principle Other
Data sources, treatment and representativeness
Data treatment and extrapolations principles no extrapolation
Percentage supply or production covered 90.0 %
Annual supply or production volume 1,800 Kt in 2010 (share of APA members is at least 90% of European production)
Sampling procedure literature values based on European company surveys & European statistics
Uncertainty adjustments none
Completeness
Completeness of product model No statement
Completeness elementary flows, per topic
  • Climate change: No statement
  • Ozone depletion: No statement
  • Summer smog: No statement
  • Eutrophication: No statement
  • Acidification: No statement
  • Human toxicity: No statement
  • Freshwater ecotoxicity: No statement
  • Seawater eco-toxicity: No statement
  • Terrestric eco-toxicity: No statement
  • Radioactivity: No statement
  • Land use: No statement
  • Non-renewable material resource depletion: No statement
  • Renewable material resource consumption: No statement
  • Non-renewable primary energy depletion: No statement
  • Renewable primary energy consumption: No statement
  • Particulate matter/respiratory inorganics: No statement
  • Species depletion: No statement
  • Noise: No statement
Validation
Type of review Scope / Method(s) of review Review details
Not reviewed
Scope name Method name
LCIA results calculation
No records found.
LCIA results
No records found.
Raw data
No records found.
Unit process(es), black box
No records found.
LCI results or Partly terminated system
No records found.
Goal and scope definition
No records found.
Documentation
No records found.
Life cycle inventory methods
No records found.
Unit process(es), single operation
No records found.
external review passed
Subsequent review comments
The goal and scope of this Eco-profile study was confirmed to be a European production average of the following polymer precursors: benzene, toluene, and ortho-, para-, and mixed xylenes (BTX). The geographical scope includes the EU 27 member states and Norway. Benchmarking data for 50 European steam cracker units were complemented by a desktop study of upstream operations (extraction, refinery), aromatics separation unit, and alternative routes (catalytic reformer, hydrodealkylation). The technological scope probably differs somewhat from the previous versions of the BTX Eco-profiles published by PlasticsEurope which had presumably been limited to catalytic reforming, but were insufficiently transparent on this issue. The main data source used for this study was a validated confidential report by the petrochemical industry (APPE) under the European Emission Trading Scheme (ETS) on energy use and CO2 emissions of European steamcracking operations. Other processes, including refinery, catalytic reformer, and hydr0dealkylation, were derived from proprietary models (developed by the practitioner IFEU through various petrochemical industry projects). Further, publicly available literature data were used. The review confirmed that, despite no primary data was collected, the data used are applicable, up-to-date, and modelled with a view to internal consistency. The temporal scope was confirmed to be 2010 as reference year and valid at least until 2014 in view of the slow technological changes. The following aspects were subject to particular scrutiny by the review panel: • The shares of the alternative routes: extraction from pyrolysis gasoline, catalytic reforming of naphtha, HDA of toluene, coking and HDA of other aromatics; • the modelling of raffinate (saturated hydrocarbons) as by-product; • the differences in specific resource use and emissions assigned to the various BTX; • the consistent and justifiable use of allocation methods; • plausibility checks of calculations along the productions chains. A review meeting between the LCA practitioner and the reviewers was held, including a model and database review, and spot checks of data and calculations. The results are thus held to be representative and reliable for the specified production routes. It is noteworthy that, compared with previous studies under the PlasticsEurope Eco-profiles programme, the results for benzene and mixed xylenes have changed notably: • The previous edition of the Eco-profiles for cracker products apparently used a mass allocation of energy demand and emissions of the steam cracking process to all cracker output streams (thus lowering specific burdens), not only to the HVC as in the present version; from today’s perspective, also to ensure consistency with current industry practice (APPE), the allocation used here is deemed more appropriate. • According to recent industry data (APPE), benzene is predominantly (approx. 60%) produced from pygas, whereas other aromatics are predominantly (>70%) produced from reformate. Since the pygas route has higher burdens than the reformer route, indicators for benzene have increased. • Conversely, mixed xylenes were shown to require less steam for separation than o- and p-xylene. As a result, the indicators for mixed xylenes have decreased. • It is noteworthy that fuel-grade by-products, specifically raffinate (saturated hydrocarbons), were calculated with their calorific value and with their upstream burdens (oil extraction, transport and refining), but no process-related environmental impacts were assigned to them. Process-related burdens (steamcracking, aromatics separation) were only allocated to the high-value BTX compounds. • The overall levels of greenhouse gas emissions of the steam cracker and aromatics units were confirmed to be in line with APPE’s ETS reporting and internal reports. For greenhouse gas emissions, the results of this new version of the Eco-profile are quite in line with the previous versions of 2005 (with the noteworthy exception of benzene and mixed xylenes discussed above). • Other impact categories changed somewhat in proportion with the process energy requirements. It should be noted, however, that some indicators apparently changed substantially due to life cycle inventory items in the previous version not being specific enough to allow an accurate a posteriori calculation (average characterisation factors applied to unspecified substance flows). In these cases, a comparison with the previous version is strictly speaking not valid. Further, the review verified that the model and calculations comply with the rules of the PlasticsEurope Eco-profiles methodology and with ISO 14040–14044: the resulting life cycle inventory datasets for benzene, tolu-ene, and o-, p-, and mixed xylenes (BTX) are thus compatible building blocks for use in other Eco-profile calculations. Review Summary The Eco-profile of benzene, toluene, and ortho-, para-, and mixed xylenes (BTX) has been validated to appropriately represent current European production of these polymer precursors. The underlying emission data for the steam cracking process are consistent with reports of the petrochemical industry under the European Emission Trading Scheme (ETS). Other processes, including refinery, catalytic reformer, and hydr0dealkylation were derived from project and literature data and modelled with a view to internal consistency. The results are thus held to be representative and reliable for the specified production routes. Reviewer Names and Institutions Chair: Dr.-Ing. Ivo Mersiowsky – Business Line Manager, Sustainability Leadership, DEKRA Consulting GmbH, Stuttgart, Germany Co-reviewer: Dr. Martin Patel – Copernicus Institute of Sustainable Development, Utrecht University, Utrecht, The Netherlands
Reviewer name and institution
Data generator
Data set generator / modeller
Data entry by
Time stamp (last saved) 2019-06-01T00:00:00.000
Data set format(s)
Data entry by
Publication and ownership
UUID 8bc19bf7-47b5-43b3-a7f8-2634b8f2fde5
Date of last revision 2019-06-01T00:00:00.000
Data set version 00.00.001
Workflow and publication status Working draft
Unchanged re-publication of
Copyright Yes
License type Free of charge for all users and uses

Inputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Elementary flow 0.0090782 kg0.0090782 kg
Elementary flow 0.029128 m30.029128 m3
Elementary flow 1.1256E-12 kg1.1256E-12 kg
Elementary flow 1.9283E-5 kg1.9283E-5 kg
Elementary flow 2.2306E-8 kg2.2306E-8 kg
Elementary flow 2.9515E-10 kg2.9515E-10 kg
Elementary flow 0.0013484 kg0.0013484 kg
Elementary flow 3.1736E-5 m2*a3.1736E-5 m2*a
Elementary flow 0.0013578 m2*a0.0013578 m2*a
Elementary flow 1.2081E-8 m31.2081E-8 m3
Elementary flow 1.0048E-4 m31.0048E-4 m3
Elementary flow 3.0432E-18 kg3.0432E-18 kg
Elementary flow 7.104472807E-7 m37.104472807E-7 m3
Elementary flow 1.2546E-10 kg1.2546E-10 kg
Elementary flow 0.2872584 MJ0.2872584 MJ
Elementary flow 3.5962E-18 kg3.5962E-18 kg
Elementary flow 1.6952E-6 m21.6952E-6 m2
Elementary flow 0.99374 m30.99374 m3
Elementary flow 1.4673E-8 kg1.4673E-8 kg
Elementary flow 0.078852 MJ0.078852 MJ
Elementary flow 2.3325E-7 kg2.3325E-7 kg
Elementary flow 3.9084E-6 kg3.9084E-6 kg
Elementary flow 7.2572E-7 m37.2572E-7 m3
Elementary flow 3.568E-9 kg3.568E-9 kg
Elementary flow 3.1367E-17 kg3.1367E-17 kg
Elementary flow 4.6076E-6 kg4.6076E-6 kg
Elementary flow 2.7058E-7 m32.7058E-7 m3
Elementary flow 5.9054E-9 m25.9054E-9 m2
Elementary flow 2.035E-6 kg2.035E-6 kg
Elementary flow 2.216055E-8 kg2.216055E-8 kg
Elementary flow 3.3628E-8 kg3.3628E-8 kg
Elementary flow 4.2821E-7 kg4.2821E-7 kg
Elementary flow 4.71492E-8 kg4.71492E-8 kg
Elementary flow 1.36003E-10 kg1.36003E-10 kg
Elementary flow 2.3232E-6 m22.3232E-6 m2
Elementary flow 1.6765E-15 kg1.6765E-15 kg
Elementary flow 5.1648E-7 m25.1648E-7 m2
Elementary flow 5.697E-6 kg5.697E-6 kg
Elementary flow 2.8445E-6 kg2.8445E-6 kg
Elementary flow 1.233E-8 kg1.233E-8 kg
Elementary flow 3.70758E-8 kg3.70758E-8 kg
Elementary flow 2.0395E-7 kg2.0395E-7 kg
Elementary flow 1.163E-9 m31.163E-9 m3
Elementary flow 2.5461E-9 kg2.5461E-9 kg
Elementary flow 6.748775001156397E-6 kg6.748775001156397E-6 kg
Elementary flow 4.406225909425611E-6 kg4.406225909425611E-6 kg
Elementary flow 0.019591 MJ0.019591 MJ
Elementary flow 8.20762918E-7 kg8.20762918E-7 kg
Elementary flow 1.8676E-11 kg1.8676E-11 kg
Elementary flow 4.4109E-9 kg4.4109E-9 kg
Elementary flow 0.05690365919 MJ0.05690365919 MJ
Elementary flow 3.77511E-12 kg3.77511E-12 kg
Elementary flow 2.3120609E-17 kg2.3120609E-17 kg
Elementary flow 7.732E-9 kg7.732E-9 kg
Elementary flow 2.01E-5 kg2.01E-5 kg
Elementary flow 2.945E-10 m32.945E-10 m3
Elementary flow 3.2575E-6 kg3.2575E-6 kg
Elementary flow 2.8807E-8 kg2.8807E-8 kg
Elementary flow 2.4857E-6 kg2.4857E-6 kg
Elementary flow 0.00247835183333333 MJ0.00247835183333333 MJ
Elementary flow 0.37822029689859354 MJ0.37822029689859354 MJ
Elementary flow 3.9918E-6 kg3.9918E-6 kg
Elementary flow 4.21681E-12 kg4.21681E-12 kg
Elementary flow 7.415E-5 kg7.415E-5 kg
Elementary flow 1.1634E-6 m21.1634E-6 m2
Elementary flow 0.0015371 MJ0.0015371 MJ
Elementary flow 2.0763E-9 kg2.0763E-9 kg
Elementary flow 6.27042E-17 kg6.27042E-17 kg
Elementary flow 0.5278672 MJ0.5278672 MJ
Elementary flow 6.259456444204204 MJ6.259456444204204 MJ
Elementary flow 1.4775E-4 m2*a1.4775E-4 m2*a
Elementary flow 1.449875308212E-18 kg1.449875308212E-18 kg
Elementary flow 1.7759E-6 m21.7759E-6 m2
Elementary flow 2.5966E-11 kg2.5966E-11 kg
Elementary flow 3.2269E-4 MJ3.2269E-4 MJ
Elementary flow 7.9109E-15 kg7.9109E-15 kg
Elementary flow 52.6761898630419 MJ52.6761898630419 MJ
Elementary flow 1.9399E-15 kg1.9399E-15 kg
Elementary flow 1.0975E-9 kg1.0975E-9 kg
Elementary flow 1.9477E-13 kg1.9477E-13 kg
Elementary flow 1.2753E-9 kg1.2753E-9 kg
Elementary flow 9.6546E-7 kg9.6546E-7 kg
Elementary flow 3.5957E-10 kg3.5957E-10 kg
Elementary flow 9.7814E-7 kg9.7814E-7 kg
Elementary flow 1.3456E-14 kg1.3456E-14 kg
Elementary flow 5.1098E-10 kg5.1098E-10 kg
Elementary flow 0.78938 kg0.78938 kg
Elementary flow 2.9368E-14 kg2.9368E-14 kg
Elementary flow 0.0019577 kg0.0019577 kg
Elementary flow 2.2805E-17 kg2.2805E-17 kg
Elementary flow 2.0817E-6 m22.0817E-6 m2
Elementary flow 2.7442E-4 m32.7442E-4 m3
Elementary flow 9.0957E-16 kg9.0957E-16 kg
Elementary flow 3.7028E-9 kg3.7028E-9 kg
Elementary flow 8.279292E-6 MJ8.279292E-6 MJ
Elementary flow 2.0241E-14 kg2.0241E-14 kg
Elementary flow 1.5446E-10 kg1.5446E-10 kg
Elementary flow 8.2953E-9 kg8.2953E-9 kg
Elementary flow 2.4588E-9 kg2.4588E-9 kg

Outputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Elementary flow 1.0131E-7 kg1.0131E-7 kg
Elementary flow 9.2781E-8 kg9.2781E-8 kg
Elementary flow 0.0037373 kg0.0037373 kg
Elementary flow 1.2109E-10 kg1.2109E-10 kg
Elementary flow 2.0388E-11 kg2.0388E-11 kg
Elementary flow 1.2026E-15 kg1.2026E-15 kg
Elementary flow 7.9323E-9 kg7.9323E-9 kg
Elementary flow 8.3891E-8 kg8.3891E-8 kg
Elementary flow 2.8019E-5 kg2.8019E-5 kg
Elementary flow 3.62956E-7 kg3.62956E-7 kg
Elementary flow 9.0359E-14 kg9.0359E-14 kg
Elementary flow 1.2623E-7 kg1.2623E-7 kg
Elementary flow 5.6584E-13 kg5.6584E-13 kg
Waste flow 2.390408E-4 kg2.390408E-4 kg
Elementary flow 8.2731E-15 kg8.2731E-15 kg
Elementary flow 0.0021491 kg0.0021491 kg
Elementary flow 9.1406E-18 kg9.1406E-18 kg
Elementary flow 5.596E-6 kg5.596E-6 kg
Elementary flow 1.0559E-6 kBq1.0559E-6 kBq
Elementary flow 1.2166E-10 kg1.2166E-10 kg
Elementary flow 1.3152E-5 kg1.3152E-5 kg
Elementary flow 1.3168E-6 kg1.3168E-6 kg
Elementary flow 3.5065E-10 kg3.5065E-10 kg
Elementary flow 1.9535E-8 kg1.9535E-8 kg
Elementary flow 3.3002E-6 kg3.3002E-6 kg
Elementary flow 3.239E-15 kg3.239E-15 kg
Elementary flow 1.0926E-9 kg1.0926E-9 kg
Elementary flow 2.0629E-6 kg2.0629E-6 kg
Elementary flow 8.04210032971E-6 kBq8.04210032971E-6 kBq
Elementary flow 2.8045E-8 kg2.8045E-8 kg
Elementary flow 9.471E-11 kg9.471E-11 kg
Elementary flow 8.0241E-15 kg8.0241E-15 kg
Elementary flow 2.9046E-7 kg2.9046E-7 kg
Elementary flow 7.2067E-12 kg7.2067E-12 kg
Elementary flow 7.7218E-12 kg7.7218E-12 kg
Elementary flow 3.2155E-20 kg3.2155E-20 kg
Elementary flow 0.0159615 kg0.0159615 kg
Elementary flow 1.942E-7 kg1.942E-7 kg
Elementary flow 2.4859E-6 kg2.4859E-6 kg
Elementary flow 9.6696E-20 kg9.6696E-20 kg
Elementary flow 1.3369E-13 kg1.3369E-13 kg
Elementary flow 1.6669E-6 kg1.6669E-6 kg
Elementary flow 5.7705E-10 kg5.7705E-10 kg
Elementary flow 4.3541E-8 kg4.3541E-8 kg
Elementary flow 9.6099E-8 kg9.6099E-8 kg
Elementary flow 2.90299E-4 kg2.90299E-4 kg
Elementary flow 1.652E-7 kg1.652E-7 kg
Elementary flow 5.0477E-10 kg5.0477E-10 kg
Elementary flow 1.0983E-13 kg1.0983E-13 kg
Elementary flow 0.0093776 kg0.0093776 kg
Elementary flow 1.7815E-7 kg1.7815E-7 kg
Elementary flow 2.4636E-7 kg2.4636E-7 kg
Elementary flow 2.2503E-5 kg2.2503E-5 kg
Elementary flow 2.8249E-10 kg2.8249E-10 kg
Elementary flow 4.7456E-11 kg4.7456E-11 kg
Elementary flow 1.5017E-7 kg1.5017E-7 kg
Elementary flow 6.9878E-10 kg6.9878E-10 kg
Elementary flow 4.5212E-16 kg4.5212E-16 kg
Elementary flow 1.5389 MJ1.5389 MJ
Elementary flow 6.2412E-21 kg6.2412E-21 kg
Elementary flow 1.0159E-13 kg1.0159E-13 kg
Elementary flow 5.2667E-10 kBq5.2667E-10 kBq
Elementary flow 1.2225E-17 kg1.2225E-17 kg
Elementary flow 3.4028E-7 kg3.4028E-7 kg
Elementary flow 1.9694E-8 kg1.9694E-8 kg
Elementary flow 4.1169E-7 kg4.1169E-7 kg
Elementary flow 1.0171E-14 kg1.0171E-14 kg
Elementary flow 9.5716E-6 kg9.5716E-6 kg
Elementary flow 7.9387E-6 kg7.9387E-6 kg
Elementary flow 2.78166E-7 kg2.78166E-7 kg
Elementary flow 3.2397E-7 kg3.2397E-7 kg
Elementary flow 4.5788E-8 kBq4.5788E-8 kBq
Elementary flow 5.9093E-4 kBq5.9093E-4 kBq
Elementary flow 2.1213E-9 kBq2.1213E-9 kBq
Elementary flow 0.0030087 kg0.0030087 kg
Elementary flow 3.2156E-14 kg3.2156E-14 kg
Elementary flow 6.039E-8 kg6.039E-8 kg
Elementary flow 4.9522E-8 kg4.9522E-8 kg
Elementary flow 4.4284E-15 kg4.4284E-15 kg
Elementary flow 2.0722E-16 kg2.0722E-16 kg
Elementary flow 5.1919E-9 kg5.1919E-9 kg
Elementary flow 4.1446E-5 kg4.1446E-5 kg
Elementary flow 2.8098E-8 kg2.8098E-8 kg
Elementary flow 1.4349E-7 kBq1.4349E-7 kBq
Elementary flow 6.3684E-7 kg6.3684E-7 kg
Elementary flow 7.727E-12 kg7.727E-12 kg
Elementary flow 3.0766E-10 kBq3.0766E-10 kBq
Elementary flow 1.7771E-7 kg1.7771E-7 kg
Elementary flow 9.3056E-6 kg9.3056E-6 kg
Elementary flow 2.2831E-16 kg2.2831E-16 kg
Elementary flow 1.8632E-4 kg1.8632E-4 kg
Waste flow 2.0861E-11 kg2.0861E-11 kg
Elementary flow 1.6285E-5 kg1.6285E-5 kg
Elementary flow 2.2105E-8 kg2.2105E-8 kg
Elementary flow 3.2463E-8 kBq3.2463E-8 kBq
Elementary flow 9.3705E-8 kBq9.3705E-8 kBq
Elementary flow 7.5498E-10 kg7.5498E-10 kg
Elementary flow 2.6841E-16 kg2.6841E-16 kg
Elementary flow 2.4551E-11 kg2.4551E-11 kg
Elementary flow 57.991 kBq57.991 kBq
Elementary flow 1.8545E-6 kg1.8545E-6 kg
Elementary flow 2.933E-6 kg2.933E-6 kg
Elementary flow 8.2924E-14 kg8.2924E-14 kg
Elementary flow 1.5113E-7 kg1.5113E-7 kg
Elementary flow 1.1244E-9 kg1.1244E-9 kg
Elementary flow 5.1069E-15 kg5.1069E-15 kg
Elementary flow 1.1703E-4 kg1.1703E-4 kg
Elementary flow 0.0040593 kBq0.0040593 kBq
Elementary flow 7.7579E-9 kg7.7579E-9 kg
Elementary flow 5.3254E-6 kg5.3254E-6 kg
Elementary flow 1.2148E-9 kg1.2148E-9 kg
Elementary flow 2.4491E-9 kBq2.4491E-9 kBq
Elementary flow 6.3714E-8 kg6.3714E-8 kg
Elementary flow 1.8365E-7 kg1.8365E-7 kg
Elementary flow 3.3125E-9 kg3.3125E-9 kg
Elementary flow 3.378E-6 kg3.378E-6 kg
Elementary flow 1.1216E-15 kg1.1216E-15 kg
Elementary flow 7.0302E-11 kg7.0302E-11 kg
Elementary flow 6.8042E-7 kg6.8042E-7 kg
Elementary flow 1.2529E-7 kBq1.2529E-7 kBq
Elementary flow 6.9536E-8 kg6.9536E-8 kg
Elementary flow 2.6456E-5 kg2.6456E-5 kg
Elementary flow 1.9297E-13 kg1.9297E-13 kg
Elementary flow 3.1477E-6 kg3.1477E-6 kg
Elementary flow 8.6516E-6 kBq8.6516E-6 kBq
Elementary flow 3.5325E-10 kg3.5325E-10 kg
Elementary flow 6.1508E-6 kg6.1508E-6 kg
Elementary flow 1.3978E-9 kg1.3978E-9 kg
Elementary flow 2.3117E-5 kg2.3117E-5 kg
Elementary flow 1.7757E-10 kg1.7757E-10 kg
Elementary flow 1.2148E-4 kg1.2148E-4 kg
Elementary flow 4.3516E-10 kg4.3516E-10 kg
Elementary flow 3.7859E-16 kg3.7859E-16 kg
Elementary flow 2.5797E-10 kg2.5797E-10 kg
Elementary flow 7.29657699E-8 kg7.29657699E-8 kg
Elementary flow 1.8744E-5 kg1.8744E-5 kg
Elementary flow 2.0734E-7 kg2.0734E-7 kg
Elementary flow 0.001539603605 kg0.001539603605 kg
Elementary flow 2.1218E-9 kg2.1218E-9 kg
Elementary flow 2.0581E-8 kg2.0581E-8 kg
Elementary flow 9.9053E-11 kg9.9053E-11 kg
Elementary flow 1.1337E-5 kBq1.1337E-5 kBq
Elementary flow 2.4951E-16 kg2.4951E-16 kg
Elementary flow 7.1805E-16 kg7.1805E-16 kg
Elementary flow 6.6753E-16 kg6.6753E-16 kg
Elementary flow 4.2943E-11 kg4.2943E-11 kg
Elementary flow 6.8865E-5 kg6.8865E-5 kg
Elementary flow 1.2753E-5 kg1.2753E-5 kg
Waste flow 2.9473E-4 kg2.9473E-4 kg
Elementary flow 1.8092E-11 kg1.8092E-11 kg
Elementary flow 1.3005E-4 kBq1.3005E-4 kBq
Elementary flow 7.0954E-7 kg7.0954E-7 kg
Elementary flow 6.6316E-8 kg6.6316E-8 kg
Elementary flow 0.039804 kg0.039804 kg
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