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Process Data set: Ethylene oxide; 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
Ethylene oxide; production mix, at plant
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 2014
Time representativeness description time to which data mainly refer: 2008 - 2010
Technological representativeness
Technology description including background system Ethylene oxide (EO) is a key chemical intermediate to the manufacture of many products. The production of ethylene oxide started in 1937 with a Union Carbide process based on ethylene and air. In 1958, oxygen (rather than air) processes were introduced by Shell Development Company, and most European EO plants are now based on pure oxygen feedstock. Ethylene glycols are produced by reacting EO with water. About 40 % of the EO production in Europe is converted into glycols. Globally the figure is even higher by about 70 % (BREF 2003). Therefore EO and ethylene glycols are mostly produced together at integrated plants. The main product is monoethylene glycol (MEG), but diethylene glycol (DEG) and triethylene glycol (TEG) are also produced. MEG is mainly used for the manufacture of polyester fibres and polyethylene terephthalate (PET), and some as antifreeze in cooling systems. DEG is used in the fibre industry and as tobacco humectant and TEG is used in the manufacture of cellophane for food packaging. DEG and TEG are both used for gas drying. In practice most EO / EG plants are designed as integrated plants for a production mix of high purity ethylene oxide and glycols. Although there is a number of different EO / EG manufacturing process licensors, the process technologies are broadly similar. Feedstock ethylene is typically received by pipeline from a steam cracker. The oxygen is regularly provided in pure form by pipeline from an air separation unit. The reaction between ethylene and oxygen is carried out in a multi-tubular fixed bed type reactor with a silver oxide catalyst in the tubes and a coolant on the shell side. The heat generated by the exothermic reactions is removed by the coolant, and is recovered by producing steam. The steam is used as a heating medium in various sections of the plant.
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 80.0 %
Annual supply or production volume 2,575 Kt in 2010 (share is estimated with at least 80% 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
Documentation
No records found.
LCIA results
No records found.
Unit process(es), single operation
No records found.
LCIA results calculation
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.
Life cycle inventory methods
No records found.
Raw data
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: Ethylene, Propylene, Butadiene, Pyrolysis Gasoline, Ethylene Oxide (EO), and Ethylene Glycols (MEG, DEG, TEG). The geographical scope includes the EU 27 member states and Norway, with a coverage of 50 plants (approx. 92% of European production volume). One important limitation of the technological scope is that the study considered only steam cracking, the most important process to produce ethylene and propylene, whereas the Fluid Catalytic Cracking (FCC) process is not included here. This technological scope is in line with earlier Eco-profiles published by PlasticsEurope which were also limited to steam crackers as a source of olefins and their derivatives. Further, since naphtha is the most common feedstock in Europe, the examined population of cracker units comprised predominantly naphtha crackers (only 2 gas crackers, while most units use a mix of feeds). 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. In addition, publicly available literature was used. Other processes, including refinery, ethylene oxidation, and ethylene glycol production, were derived from a proprietary refinery model (developed by the practitioner IFEU through various petrochemical industry projects), and further literature data. The review confirmed that, despite no primary data collection was conducted, the data used are applicable, up-todate, and modelled with a view to internal consistency. The temporal scope was confirmed to be 2009 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 product range of the steam cracker, especially the designation as high value compounds (HVC) for the purposes of allocation; •the input/output balance of hydrocarbon feedstocks, also accounting for internal loops or further processing of some intermediate products (such as hydrogen and pyrolysis gas); •specifically, the modelling of non-HVC refinery/fuel gases which are valorised either for thermal energy or for secondary cracking or other post-processing steps – while these will not be burdened with process energy requirements and emissions of the steam cracker itself, they do bear a share of the upstream burdens; •the use of electric and thermal energy, and the consistent accounting for the associated emissions; •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 Ecoprofiles programme, the results for butadiene and pyrolysis gasoline (pygas) have changed notably: •According to recent industry data (APPE), the thermal energy (steam) required for the steam cracking process is rather high compared with the previous version of this Eco-profile. •The previous edition of the Eco-profiles for olefins apparently used a mass allocation for 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 latter allocation is deemed more appropriate. •It is noteworthy that fuel-grade by-products which are returned to the refinery (looped back) 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. •Specifically, the impact indicators for butadiene have increased substantially because butadiene is extracted in a separate facility following the steam cracker, and this additional processing requires thermal energy, electricity, and solvents. •The impact indicators for pygas (including benzene, toluene and xylene, BTX, and other components) have decreased because of the adjusted allocation. •The overall levels of greenhouse gas emissions of the steam cracker units were confirmed to be in line with APPE’s ETS reporting and corroborated by bottom-up calculations based on the internal use of low-value byproducts as process fuels (mainly methane). For greenhouse gas emissions, the results of this new version of the Eco-profile are hardly higher than those published in the previous version of 2005. •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 Ecoprofiles methodology and with ISO 14040–14044: the resulting life cycle inventory datasets for Ethylene, Propylene, Butadiene, Pyrolysis Gasoline, Ethylene Oxide (EO), and Ethylene Glycols (MEG, DEG, TEG) and are thus compatible building blocks for use in other Eco-profile calculations. Review Summary The Eco-profile of Ethylene, Propylene, Butadiene, Pyrolysis Gasoline, Ethylene Oxide (EO), and Ethylene Glycols (MEG, DEG, TEG) 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, ethylene oxidation, and ethylene glycol production, 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 361a30a2-2521-15e9-c613-000071c7496a
Date of last revision 2019-06-01T00:00:00.000
Data set version 00.00.001
Workflow and publication status Working draft
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 0.096265 kg0.096265 kg
Elementary flow 0.0365346 m30.0365346 m3
Elementary flow 9.253E-13 kg9.253E-13 kg
Elementary flow 1.3679E-5 kg1.3679E-5 kg
Elementary flow 1.391E-8 kg1.391E-8 kg
Elementary flow 2.1845E-10 kg2.1845E-10 kg
Elementary flow 6.6762E-4 kg6.6762E-4 kg
Elementary flow 2.6164E-5 m2*a2.6164E-5 m2*a
Elementary flow 0.014633 m2*a0.014633 m2*a
Elementary flow 1.1827E-8 m31.1827E-8 m3
Elementary flow 5.0701E-4 m35.0701E-4 m3
Elementary flow 2.5206E-18 kg2.5206E-18 kg
Elementary flow 6.037252002E-7 m36.037252002E-7 m3
Elementary flow 1.0214E-10 kg1.0214E-10 kg
Elementary flow 1.4645664 MJ1.4645664 MJ
Elementary flow 2.9783E-18 kg2.9783E-18 kg
Elementary flow 1.4345E-6 m21.4345E-6 m2
Elementary flow 0.80376 m30.80376 m3
Elementary flow 2.4893E-8 kg2.4893E-8 kg
Elementary flow 0.46647 MJ0.46647 MJ
Elementary flow 1.9011E-7 kg1.9011E-7 kg
Elementary flow 3.301E-6 kg3.301E-6 kg
Elementary flow 7.8387E-7 m37.8387E-7 m3
Elementary flow 2.2372E-9 kg2.2372E-9 kg
Elementary flow 2.5978E-17 kg2.5978E-17 kg
Elementary flow 2.8952E-6 kg2.8952E-6 kg
Elementary flow 2.2988E-7 m32.2988E-7 m3
Elementary flow 4.835E-9 m24.835E-9 m2
Elementary flow 1.271E-6 kg1.271E-6 kg
Elementary flow 2.148198E-8 kg2.148198E-8 kg
Elementary flow 2.1086E-8 kg2.1086E-8 kg
Elementary flow 2.6856E-7 kg2.6856E-7 kg
Elementary flow 3.14576E-8 kg3.14576E-8 kg
Elementary flow 1.11857E-10 kg1.11857E-10 kg
Elementary flow 1.933E-6 m21.933E-6 m2
Elementary flow 1.3568E-15 kg1.3568E-15 kg
Elementary flow 4.1845E-7 m24.1845E-7 m2
Elementary flow 4.8111E-6 kg4.8111E-6 kg
Elementary flow 3.383E-5 kg3.383E-5 kg
Elementary flow 9.7509E-9 kg9.7509E-9 kg
Elementary flow 7.94368E-8 kg7.94368E-8 kg
Elementary flow 1.2788E-7 kg1.2788E-7 kg
Elementary flow 9.6323E-10 m39.6323E-10 m3
Elementary flow 1.5965E-9 kg1.5965E-9 kg
Elementary flow 5.695046500952088E-6 kg5.695046500952088E-6 kg
Elementary flow 3.718254150269751E-6 kg3.718254150269751E-6 kg
Elementary flow 0.16137 MJ0.16137 MJ
Elementary flow 5.39721E-7 kg5.39721E-7 kg
Elementary flow 1.5054E-11 kg1.5054E-11 kg
Elementary flow 3.6533E-9 kg3.6533E-9 kg
Elementary flow 0.5715005397 MJ0.5715005397 MJ
Elementary flow 3.10491E-12 kg3.10491E-12 kg
Elementary flow 1.9124511E-17 kg1.9124511E-17 kg
Elementary flow 6.3322E-9 kg6.3322E-9 kg
Elementary flow 1.6975E-5 kg1.6975E-5 kg
Elementary flow 2.4394E-10 m32.4394E-10 m3
Elementary flow 9.3405E-6 kg9.3405E-6 kg
Elementary flow 5.8268E-8 kg5.8268E-8 kg
Elementary flow 2.0621E-6 kg2.0621E-6 kg
Elementary flow 0.00204925076811594 MJ0.00204925076811594 MJ
Elementary flow 2.1584146823009993 MJ2.1584146823009993 MJ
Elementary flow 3.0058E-6 kg3.0058E-6 kg
Elementary flow 3.46812E-12 kg3.46812E-12 kg
Elementary flow 5.2214E-5 kg5.2214E-5 kg
Elementary flow 9.4552E-7 m29.4552E-7 m2
Elementary flow 0.016875 MJ0.016875 MJ
Elementary flow 1.2982E-9 kg1.2982E-9 kg
Elementary flow 5.19259E-17 kg5.19259E-17 kg
Elementary flow 2.807168 MJ2.807168 MJ
Elementary flow 9.308790565963891 MJ9.308790565963891 MJ
Elementary flow 6.5182E-4 m2*a6.5182E-4 m2*a
Elementary flow 1.20074812677E-18 kg1.20074812677E-18 kg
Elementary flow 1.451E-6 m21.451E-6 m2
Elementary flow 2.0203E-11 kg2.0203E-11 kg
Elementary flow 0.0034873 MJ0.0034873 MJ
Elementary flow 6.7734E-15 kg6.7734E-15 kg
Elementary flow 43.0106398881723 MJ43.0106398881723 MJ
Elementary flow 1.5758E-15 kg1.5758E-15 kg
Elementary flow 9.0257E-10 kg9.0257E-10 kg
Elementary flow 1.6134E-13 kg1.6134E-13 kg
Elementary flow 7.9961E-10 kg7.9961E-10 kg
Elementary flow 7.1417E-7 kg7.1417E-7 kg
Elementary flow 2.2601E-10 kg2.2601E-10 kg
Elementary flow 8.261E-7 kg8.261E-7 kg
Elementary flow 9.4694E-15 kg9.4694E-15 kg
Elementary flow 3.2039E-10 kg3.2039E-10 kg
Elementary flow 0.42281 kg0.42281 kg
Elementary flow 2.3578E-14 kg2.3578E-14 kg
Elementary flow 0.005406 kg0.005406 kg
Elementary flow 1.8887E-17 kg1.8887E-17 kg
Elementary flow 1.7398E-6 m21.7398E-6 m2
Elementary flow 2.2743E-4 m32.2743E-4 m3
Elementary flow 6.5029E-16 kg6.5029E-16 kg
Elementary flow 2.9285E-9 kg2.9285E-9 kg
Elementary flow 1.464792E-5 MJ1.464792E-5 MJ
Elementary flow 1.6767E-14 kg1.6767E-14 kg
Elementary flow 1.2784E-10 kg1.2784E-10 kg
Elementary flow 7.586E-9 kg7.586E-9 kg
Elementary flow 1.8089E-9 kg1.8089E-9 kg

Outputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Elementary flow 3.1285E-7 kg3.1285E-7 kg
Elementary flow 9.2034E-8 kg9.2034E-8 kg
Elementary flow 0.0036896 kg0.0036896 kg
Elementary flow 9.1122E-11 kg9.1122E-11 kg
Elementary flow 1.6E-11 kg1.6E-11 kg
Elementary flow 9.8724E-16 kg9.8724E-16 kg
Elementary flow 6.5542E-9 kg6.5542E-9 kg
Elementary flow 4.6735E-8 kg4.6735E-8 kg
Elementary flow 2.9943E-4 kg2.9943E-4 kg
Elementary flow 9.0128E-7 kg9.0128E-7 kg
Elementary flow 7.5437E-14 kg7.5437E-14 kg
Elementary flow 1.0507E-7 kg1.0507E-7 kg
Elementary flow 4.6327E-13 kg4.6327E-13 kg
Waste flow 9.1241E-4 kg9.1241E-4 kg
Elementary flow 6.8105E-15 kg6.8105E-15 kg
Elementary flow 0.0029447 kg0.0029447 kg
Elementary flow 7.3647E-18 kg7.3647E-18 kg
Elementary flow 6.9167E-6 kg6.9167E-6 kg
Elementary flow 1.2677E-5 kBq1.2677E-5 kBq
Elementary flow 1.4606E-9 kg1.4606E-9 kg
Elementary flow 8.0778E-6 kg8.0778E-6 kg
Elementary flow 1.5521E-6 kg1.5521E-6 kg
Elementary flow 5.2354E-11 kg5.2354E-11 kg
Elementary flow 1.6477E-8 kg1.6477E-8 kg
Elementary flow 2.8886E-6 kg2.8886E-6 kg
Elementary flow 2.8548E-15 kg2.8548E-15 kg
Elementary flow 9.2856E-10 kg9.2856E-10 kg
Elementary flow 2.7036E-6 kg2.7036E-6 kg
Elementary flow 9.65540039337E-5 kBq9.65540039337E-5 kBq
Elementary flow 2.2628E-8 kg2.2628E-8 kg
Elementary flow 4.5723E-10 kg4.5723E-10 kg
Elementary flow 6.5338E-15 kg6.5338E-15 kg
Elementary flow 1.263E-7 kg1.263E-7 kg
Elementary flow 5.4014E-12 kg5.4014E-12 kg
Elementary flow 5.9363E-12 kg5.9363E-12 kg
Elementary flow 2.3518E-20 kg2.3518E-20 kg
Elementary flow 0.0131919 kg0.0131919 kg
Elementary flow 1.5995E-7 kg1.5995E-7 kg
Elementary flow 6.1027E-6 kg6.1027E-6 kg
Elementary flow 7.6227E-20 kg7.6227E-20 kg
Elementary flow 1.0947E-13 kg1.0947E-13 kg
Elementary flow 4.1411E-6 kg4.1411E-6 kg
Elementary flow 3.6296E-10 kg3.6296E-10 kg
Elementary flow 1.5564E-8 kg1.5564E-8 kg
Elementary flow 2.9444E-8 kg2.9444E-8 kg
Elementary flow 3.61251E-4 kg3.61251E-4 kg
Elementary flow 5.4219E-7 kg5.4219E-7 kg
Elementary flow 8.7615E-11 kg8.7615E-11 kg
Elementary flow 9.2178E-14 kg9.2178E-14 kg
Elementary flow 0.095027 kg0.095027 kg
Elementary flow 6.1997E-8 kg6.1997E-8 kg
Elementary flow 2.9578E-6 kg2.9578E-6 kg
Elementary flow 2.821E-5 kg2.821E-5 kg
Elementary flow 2.3356E-10 kg2.3356E-10 kg
Elementary flow 4.0332E-11 kg4.0332E-11 kg
Elementary flow 3.7301E-7 kg3.7301E-7 kg
Elementary flow 3.2121E-9 kg3.2121E-9 kg
Elementary flow 5.4859E-16 kg5.4859E-16 kg
Elementary flow 8.3615 MJ8.3615 MJ
Elementary flow 1.0645E-20 kg1.0645E-20 kg
Elementary flow 8.2126E-14 kg8.2126E-14 kg
Elementary flow 7.7338E-9 kBq7.7338E-9 kBq
Elementary flow 7.6654E-18 kg7.6654E-18 kg
Elementary flow 2.7941E-7 kg2.7941E-7 kg
Elementary flow 1.6611E-8 kg1.6611E-8 kg
Elementary flow 1.1381E-7 kg1.1381E-7 kg
Elementary flow 8.3466E-15 kg8.3466E-15 kg
Elementary flow 8.5403E-6 kg8.5403E-6 kg
Elementary flow 6.4198E-6 kg6.4198E-6 kg
Elementary flow 2.34574E-7 kg2.34574E-7 kg
Elementary flow 2.683E-7 kg2.683E-7 kg
Elementary flow 5.2319E-7 kBq5.2319E-7 kBq
Elementary flow 0.0069992 kBq0.0069992 kBq
Elementary flow 2.5434E-8 kBq2.5434E-8 kBq
Elementary flow 0.0019047 kg0.0019047 kg
Elementary flow 2.6184E-14 kg2.6184E-14 kg
Elementary flow 3.5599E-8 kg3.5599E-8 kg
Elementary flow 4.0912E-8 kg4.0912E-8 kg
Elementary flow 3.6736E-15 kg3.6736E-15 kg
Elementary flow 1.6645E-16 kg1.6645E-16 kg
Elementary flow 4.3418E-9 kg4.3418E-9 kg
Elementary flow 2.0716E-5 kg2.0716E-5 kg
Elementary flow 2.294E-8 kg2.294E-8 kg
Elementary flow 1.6068E-6 kBq1.6068E-6 kBq
Elementary flow 1.967E-7 kg1.967E-7 kg
Elementary flow 5.9405E-12 kg5.9405E-12 kg
Elementary flow 4.5177E-9 kBq4.5177E-9 kBq
Elementary flow 6.9907E-8 kg6.9907E-8 kg
Elementary flow 7.9625E-6 kg7.9625E-6 kg
Elementary flow 1.886E-16 kg1.886E-16 kg
Elementary flow 1.1864E-4 kg1.1864E-4 kg
Waste flow 2.251E-10 kg2.251E-10 kg
Elementary flow 1.7763E-4 kg1.7763E-4 kg
Elementary flow 1.5045E-8 kg1.5045E-8 kg
Elementary flow 3.8033E-7 kBq3.8033E-7 kBq
Elementary flow 1.0707E-6 kBq1.0707E-6 kBq
Elementary flow 8.4985E-9 kg8.4985E-9 kg
Elementary flow 2.1549E-16 kg2.1549E-16 kg
Elementary flow 1.9741E-11 kg1.9741E-11 kg
Elementary flow 662.65 kBq662.65 kBq
Elementary flow 1.4997E-6 kg1.4997E-6 kg
Elementary flow 2.4604E-6 kg2.4604E-6 kg
Elementary flow 1.1498E-13 kg1.1498E-13 kg
Elementary flow 7.6518E-8 kg7.6518E-8 kg
Elementary flow 9.4149E-10 kg9.4149E-10 kg
Elementary flow 4.1601E-15 kg4.1601E-15 kg
Elementary flow 1.9154E-5 kg1.9154E-5 kg
Elementary flow 0.048737 kBq0.048737 kBq
Elementary flow 6.5638E-9 kg6.5638E-9 kg
Elementary flow 1.2567E-5 kg1.2567E-5 kg
Elementary flow 1.0236E-9 kg1.0236E-9 kg
Elementary flow 2.7985E-8 kBq2.7985E-8 kBq
Elementary flow 5.1638E-8 kg5.1638E-8 kg
Elementary flow 1.5061E-7 kg1.5061E-7 kg
Elementary flow 2.6425E-9 kg2.6425E-9 kg
Elementary flow 2.5297E-6 kg2.5297E-6 kg
Elementary flow 9.0388E-16 kg9.0388E-16 kg
Elementary flow 5.7813E-11 kg5.7813E-11 kg
Elementary flow 5.329E-7 kg5.329E-7 kg
Elementary flow 1.5035E-6 kBq1.5035E-6 kBq
Elementary flow 2.1842E-8 kg2.1842E-8 kg
Elementary flow 2.1647E-5 kg2.1647E-5 kg
Elementary flow 1.5988E-13 kg1.5988E-13 kg
Elementary flow 2.6022E-6 kg2.6022E-6 kg
Elementary flow 9.6879E-5 kBq9.6879E-5 kBq
Elementary flow 8.0286E-11 kg8.0286E-11 kg
Elementary flow 6.1417E-6 kg6.1417E-6 kg
Elementary flow 1.1087E-9 kg1.1087E-9 kg
Elementary flow 1.4768E-8 kg1.4768E-8 kg
Elementary flow 1.4907E-10 kg1.4907E-10 kg
Elementary flow 4.5691E-4 kg4.5691E-4 kg
Elementary flow 5.0049E-9 kg5.0049E-9 kg
Elementary flow 3.136E-16 kg3.136E-16 kg
Elementary flow 2.0E-5 kg2.0E-5 kg
Elementary flow 8.439382729E-7 kg8.439382729E-7 kg
Elementary flow 4.64E-5 kg4.64E-5 kg
Elementary flow 2.7477E-7 kg2.7477E-7 kg
Elementary flow 0.001674989177 kg0.001674989177 kg
Elementary flow 1.8966E-9 kg1.8966E-9 kg
Elementary flow 5.6559E-9 kg5.6559E-9 kg
Elementary flow 6.2587E-11 kg6.2587E-11 kg
Elementary flow 1.2876E-4 kBq1.2876E-4 kBq
Elementary flow 2.9322E-15 kg2.9322E-15 kg
Elementary flow 5.9045E-16 kg5.9045E-16 kg
Elementary flow 5.5293E-16 kg5.5293E-16 kg
Elementary flow 3.5159E-11 kg3.5159E-11 kg
Elementary flow 5.561E-5 kg5.561E-5 kg
Elementary flow 1.2397E-5 kg1.2397E-5 kg
Waste flow 5.0172E-4 kg5.0172E-4 kg
Elementary flow 1.5154E-11 kg1.5154E-11 kg
Elementary flow 0.0015613 kBq0.0015613 kBq
Elementary flow 5.8404E-7 kg5.8404E-7 kg
Elementary flow 5.3772E-8 kg5.3772E-8 kg
Elementary flow 0.032181 kg0.032181 kg
Elementary flow 6.5259E-11 kg6.5259E-11 kg
Elementary flow 3.6549E-8 kg3.6549E-8 kg
Elementary flow 1.0536 MJ1.0536 MJ
Elementary flow 2.4925E-14 kg2.4925E-14 kg
Elementary flow 3.9049 kBq3.9049 kBq
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Elementary flow 2.9058E-5 kg2.9058E-5 kg
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