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Process Data set: containerboard production, fluting medium, semichemical, 40% recycled content | containerboard, fluting medium | Cutoff, U (en) en

Key Data Set Information
Location CL
Geographical representativeness description Data from a mill located in the province of Québec, Canada.
Reference year 2009
Name
containerboard production, fluting medium, semichemical, 40% recycled content | containerboard, fluting medium | Cutoff, U
Classification
Class name : Hierarchy level
  • ILCD: #ECOED / 2. RESIMPLE_envases / CicloData - Envases / Caja de cartón
General comment on data set ecoQuery: https://ecoquery.ecoinvent.org/3.10/cutoff/dataset/11346/documentation This dataset represents the production of semichemical fluting with a 40% recycled content intended for the production of corrugated board base paper in Québec, Canada. The mill which provided data manufactures only fluting medium, but multiple grammages. The production data represent the average of produced grammages, assuming a homogeneous production. From the reception of pulpwood, wood chips, recovered paper, fossil fuels, consumables and chemicals at the mill gate, and water input from river. This activity ends with the loading on lorries of the fluting medium intended for the production of corrugated board. The dataset includes waste paper and wood handling, semi-chemical and recycled pulp manufacturing, paper manufacturing and on-site effluent treatment, biomass combustion ash and emissions to air, effluent emissions to water, sludge and municipal waste. Fossil fuel combustion emissions to air are not directly included in this dataset but are taken into account by the heat input. NOTE: Energy from combusted fossil fuels is included in this datasets with heat inputs. Those heat inputs include material and infrastrcuture inputs and waste treatments. Therefore, a small double counting occurs, as infrastructure and electricity are already included in the dataset. Exclusions: fossil carbon dioxide emissions from make-up sodium carbonate, confidential effluent water emissions (acetaldehyde, aluminium, benzene, chromium, hexavalent chromium compound, copper, cyanides, dichloromethane, lead, mercury, methyl ethyl ketone, nickel, toluene, trichloroethylene, zinc) and carbon dioxide emissions from wastewater treatment ponds. The excluded effluent water emissions do not constitute major impact contributors to any damage category (0.6% and 0.03% for Human Health and Ecosystems respectively) using the ReCiPe Hierarchist v1.07 LCIA method.
Copyright Yes
Quantitative reference
Reference flow(s)
Time representativeness
Data set valid until 2023
Technological representativeness
LCI method and allocation
Type of data set Unit process, black box
LCI Method Principle Other
Data sources, treatment and representativeness
Data source(s) used for this data set
Sampling procedure Most data are primary data from a mill located in the province of Québec. Note on representativeness percent, value based on Québec production capacity.
Completeness
Completeness of product model No statement
Data generator
Data set generator / modeller
Data entry by
Time stamp (last saved) 2025-07-31T16:30:47.726-03:00
Data set format(s)
Data entry by
Publication and ownership
UUID 2d8d5adb-3a23-4a3c-afc1-e557e4de9344
Date of last revision 2025-07-18T12:28:03.090-03:00
Data set version 00.00.009
Copyright Yes

Inputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics GLO 3.3519300827632533E-4 kg3.3519300827632533E-4 kg
General comment 34%, 70%, 60%, 10% and 25% solution.
Product flow
C:Manufacturing / 17:Manufacture of paper and paper products / 170:Manufacture of paper and paper products / 1701:Manufacture of pulp, paper and paperboard GLO 3.2822792381478234E-5 kg3.2822792381478234E-5 kg
General comment Cores and other cardboard for packaging.
Product flow
F:Construction / 43:Specialized construction activities / 431:Demolition and site preparation / 4312:Site preparation GLO 0.03689348101714304 MJ0.03689348101714304 MJ
General comment Reported as fuel input in litres. A lower heating value of 42.8 MJ/l and a density of 0.84 kg/l were used.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals RoW 8.820510025165109E-6 kg8.820510025165109E-6 kg
General comment 5% aqueous solution.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 202:Manufacture of other chemical products / 2021:Manufacture of pesticides and other agrochemical products GLO 7.344068936069708E-5 kg7.344068936069708E-5 kg
General comment 30.3% and 50% acqueous solutions. Proxy for biocides (50% dithiocarbamate compounds and 50% glutaraldehyde).
Product flow D:Electricity, gas, steam and air conditioning supply / 35:Electricity, gas, steam and air conditioning supply / 351:Electric power generation, transmission and distribution / 3510:Electric power generation, transmission and distribution CL 2.7190591698236646 MJ2.7190591698236646 MJ
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 4.971518901092915E-5 kg4.971518901092915E-5 kg
General comment 29% aqueous solution.
Product flow
C:Manufacturing / 17:Manufacture of paper and paper products / 170:Manufacture of paper and paper products / 1701:Manufacture of pulp, paper and paperboard RoW 0.01802060343658292 MJ0.01802060343658292 MJ
General comment Propane burned in boilers. Reported as fuel input in litres. A lower heating value of 46.46 MJ/l and a fuel use of 1.0526 from underlying ecoinvent process were used.
Product flow
C:Manufacturing / 17:Manufacture of paper and paper products / 170:Manufacture of paper and paper products / 1701:Manufacture of pulp, paper and paperboard RoW 1.2348642444105213 MJ1.2348642444105213 MJ
General comment Reported as fuel input in litres. A lower heating value of 42.5 MJ/l and a fuel use of 1.133 from underlying ecoinvent process were used.
Product flow
C:Manufacturing / 17:Manufacture of paper and paper products / 170:Manufacture of paper and paper products / 1701:Manufacture of pulp, paper and paperboard RoW 0.0011342291025047012 MJ0.0011342291025047012 MJ
General comment Reported as fuel input in kg. A lower heating value of 28.9 MJ/kg and a fuel use of 1.25 from underlying ecoinvent process were used.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals RoW 2.1414788367719623E-4 kg2.1414788367719623E-4 kg
General comment 66% aqueous solution.
Product flow
C:Manufacturing / 19:Manufacture of coke and refined petroleum products / 192:Manufacture of refined petroleum products / 1920:Manufacture of refined petroleum products CL 1.7600000000000016E-4 kg1.7600000000000016E-4 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Product flow B:Mining and quarrying / 07:Mining of metal ores / 072:Mining of non-ferrous metal ores / 0729:Mining of other non-ferrous metal ores GLO 2.5673870976533727E-5 kg2.5673870976533727E-5 kg
Product flow C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 9.48129877444968E-4 kg9.48129877444968E-4 kg
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 3.5394692613084038E-6 kg3.5394692613084038E-6 kg
General comment 40% aqueous solution.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2013:Manufacture of plastics and synthetic rubber in primary forms CL 7.485941148147138E-6 kg7.485941148147138E-6 kg
General comment Felt and cloth component.
Product flow
F:Construction / 42:Civil engineering / 429:Construction of other civil engineering projects / 4290:Construction of other civil engineering projects GLO 5.434782608695655E-11 Item(s)5.434782608695655E-11 Item(s)
General comment Estimated value with lifetime (50 years) and yearly production (368 kt) of underlying ecoinvent process (integrated paper mill).
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 6.132294023057426E-6 kg6.132294023057426E-6 kg
General comment 45% aqueous solution.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2012:Manufacture of fertilizers and nitrogen compounds RoW 5.673507581332406E-7 kg5.673507581332406E-7 kg
General comment 5% aqueous solution. Proxy for sodium nitrite.
Product flow
F:Construction / 43:Specialized construction activities / 431:Demolition and site preparation / 4312:Site preparation GLO 0.002797590717069583 MJ0.002797590717069583 MJ
General comment Propane burned in lift trucks. Reported as fuel input in litres. A lower heating value of 46.46 MJ/l and a density of 0.502 kg/l was used.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals RoW 1.3816194707148914E-4 kg1.3816194707148914E-4 kg
General comment 30% solution.
Product flow
A:Agriculture, forestry and fishing / 02:Forestry and logging / 022:Logging / 0220:Logging RoW 6.142928227782626E-4 m36.142928227782626E-4 m3
General comment Purchased wood for pulping, including bark. Reported in mass. Converted in volume with a density of 623.64 kg / m3 (0% water). This wood supply was composed of aspen, birch and hardwood. Includes bark.
Product flow
A:Agriculture, forestry and fishing / 02:Forestry and logging / 022:Logging / 0220:Logging RoW 3.7041533593821634E-5 m33.7041533593821634E-5 m3
General comment Purchased wood for pulping, including bark. Proxy for low density hardwood (poplar). Reported in mass. Converted in volume with a density of 440 kg / m3 (0% water).
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals RoW 2.744973790121103E-4 kg2.744973790121103E-4 kg
General comment 50% acqueous solution and pure substance.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 0.00908488003415915 kg0.00908488003415915 kg
General comment Reported as "Soda ash (Na2CO3)".
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals RoW 5.2282348986581555E-5 kg5.2282348986581555E-5 kg
General comment 13%, 40%, 33%, 10% and 1.5% acqueous solutions.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 202:Manufacture of other chemical products / 2023:Manufacture of soap and detergents, cleaning and polishing preparations, pe RoW 1.2980022348804915E-5 kg1.2980022348804915E-5 kg
General comment 5% aqueous solution. Reported as sodium metasilicate.
Product flow
C:Manufacturing / 24:Manufacture of basic metals / 241:Manufacture of basic iron and steel / 2410:Manufacture of basic iron and steel GLO 1.4887847155978316E-4 kg1.4887847155978316E-4 kg
General comment Proxy for debarking chains.
Product flow
C:Manufacturing / 13:Manufacture of textiles / 131:Spinning, weaving and finishing of textiles / 1312:Weaving of textiles GLO 7.485941148147138E-6 kg7.485941148147138E-6 kg
General comment Felt and cloth component.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2011:Manufacture of basic chemicals GLO 1.9781417786378123E-6 kg1.9781417786378123E-6 kg
General comment 4% aqueous solution.
Product flow
C:Manufacturing / 20:Manufacture of chemicals and chemical products / 201:Manufacture of basic chemicals, fertilizers and nitrogen compounds, plastics / 2012:Manufacture of fertilizers and nitrogen compounds RoW 7.036547076573757E-5 kg7.036547076573757E-5 kg
General comment The exchange has been updated from 'urea, as N' into 'urea' and therefore its amount has been scaled (multiplied) from 0.0328 kg by 2.1438 kg of 'urea' per kg of 'urea, as N'. Original comment of the exchange is: 80% aqueous solution, CO(NH2)2. For wastewater treatment.
Product flow
Recycled content cut-off GLO 0.41742752536952843 kg0.41742752536952843 kg
General comment Multiple waste paperboard sources. Amounts reported as 5% water on a wet mass basis.
Product flow
A:Agriculture, forestry and fishing / 02:Forestry and logging / 022:Logging / 0220:Logging RoW 0.8259109863454259 kg0.8259109863454259 kg
General comment Purchased wood from sawmills (mostly) and forests for pulping and energy production. This wood supply was composed of aspen, birch, hardwood and softwood (energy production only).
Elementary flow Resources / Resources from water / Renewable material resources from water CL 0.013835963406103215 m30.013835963406103215 m3

Outputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Product flow
C:Manufacturing / 17:Manufacture of paper and paper products / 170:Manufacture of paper and paper products / 1702:Manufacture of corrugated paper and paperboard and of containers of paper a CA-QC 1.0 kg1.0 kg
General comment Net saleable product
Waste flow E:Water supply; sewerage, waste management and remediation activities / 38:Waste collection, treatment and disposal activities; materials recovery / 382:Waste treatment and disposal / 3822:Treatment and disposal of hazardous waste RoW 0.03668020313791754 kg0.03668020313791754 kg
Waste flow
E:Water supply; sewerage, waste management and remediation activities / 38:Waste collection, treatment and disposal activities; materials recovery / 382:Waste treatment and disposal / 3822:Treatment and disposal of hazardous waste CA 0.0024620024892571327 kg0.0024620024892571327 kg
General comment Reported as sludge from sodium carbonate regeneration.
Waste flow
E:Water supply; sewerage, waste management and remediation activities / 38:Waste collection, treatment and disposal activities; materials recovery / 382:Waste treatment and disposal / 3821:Treatment and disposal of non-hazardous waste CA 0.01970964723410832 kg0.01970964723410832 kg
General comment Paper-related rejects. The average dry mass of the rejects is about 30%.
Waste flow
A:Agriculture, forestry and fishing / 01:Crop and animal production, hunting and related service activities / 016:Support activities to agriculture and post-harvest crop activities / 0161:Support activities for crop production RoW 0.01700235298392882 kg0.01700235298392882 kg
General comment Primary, secondary and mixed sludges.
Waste flow
C:Manufacturing / 23:Manufacture of other non-metallic mineral products / 239:Manufacture of non-metallic mineral products n.e.c. / 2394:Manufacture of cement, lime and plaster RoW 8.999999999999999E-5 kg8.999999999999999E-5 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from those datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Waste flow
E:Water supply; sewerage, waste management and remediation activities / 38:Waste collection, treatment and disposal activities; materials recovery / 383:Materials recovery / 3830:Materials recovery RoW 1.4887847155978316E-4 kg1.4887847155978316E-4 kg
General comment Proxy for debarking chains end of life.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 4.486250034068305E-7 kg4.486250034068305E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.2723374487839913E-5 kg1.2723374487839913E-5 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 7.354664631653538E-9 kg7.354664631653538E-9 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 6.692376877163336E-6 kg6.692376877163336E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 3.677241467026424E-9 kg3.677241467026424E-9 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 4.4127079301917847E-7 kg4.4127079301917847E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 5.147947271356285E-9 kg5.147947271356285E-9 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 4.3023720621769144E-5 kg4.3023720621769144E-5 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 0.7229293287182148 kg0.7229293287182148 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.). A comparison with confidential CO2, CH4 and N2O emission factors for black liquor led to a 7% difference of CO2eq for the sum of those three greenhouse gases.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 3.530157259273393E-4 kg3.530157259273393E-4 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.3238032941775013E-6 kg1.3238032941775013E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.9123854169505732E-8 kg2.9123854169505732E-8 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.9417750038610727E-10 kg2.9417750038610727E-10 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.6179717096835717E-7 kg1.6179717096835717E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.838598021313132E-5 kg1.838598021313132E-5 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.). A comparison with confidential CO2, CH4 and N2O emission factors for black liquor led to a 7% difference of CO2eq for the sum of those three greenhouse gases.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.279896068972412E-13 kg2.279896068972412E-13 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.2063539650958923E-7 kg2.2063539650958923E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 3.677241467026424E-7 kg3.677241467026424E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 9.56092774794909E-7 kg9.56092774794909E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 5.295122327909665E-14 kg5.295122327909665E-14 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 6.692376877163336E-6 kg6.692376877163336E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.2798960689724123E-5 kg2.2798960689724123E-5 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.838598021313132E-7 kg1.838598021313132E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.6476065883550026E-6 kg2.6476065883550026E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.2502611903009812E-6 kg1.2502611903009812E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.2063539650958923E-9 kg2.2063539650958923E-9 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.941775003861073E-6 kg2.941775003861073E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.). A comparison with confidential CO2, CH4 and N2O emission factors for black liquor led to a 7% difference of CO2eq for the sum of those three greenhouse gases.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 4.412707930191784E-6 kg4.412707930191784E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 4.4127079301917844E-8 kg4.4127079301917844E-8 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 7.869323085588658E-4 kg7.869323085588658E-4 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 8.163673198695409E-8 kg8.163673198695409E-8 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 3.3830730515203535E-4 kg3.3830730515203535E-4 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 5.956955838398155E-11 kg5.956955838398155E-11 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.206353965095892E-6 kg2.206353965095892E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.7209488248707717E-4 kg1.7209488248707717E-4 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 9.560927747949089E-6 kg9.560927747949089E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 1.838598021313132E-5 kg1.838598021313132E-5 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.206353965095892E-6 kg2.206353965095892E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 0.0015336178309848915 m30.0015336178309848915 m3
General comment Calculated value considering: - sheet drying evaporation - black liquor combustion - wood residue combustion (bark, sludge)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 2.206353965095892E-6 kg2.206353965095892E-6 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified CA-QC 8.825506709183909E-7 kg8.825506709183909E-7 kg
General comment Estimation based on dry biomass (0% water) input data and emission factors from the ecoinvent 2.2 dataset "Wood chips, from industry, mixed, burned in furnace 300kW/CH U". In this case, biomass included purchased wood chips for steam production, black liquor (proxy) and wood process residues (proxy). The corresponding emissions from wood chips and residues were calculated using a bulk density of 189 kg/m3, assuming a constant lower heating value. A lower heating value of 11.2 MJ/kg on a dry mass basis was used to estimate emissions from black liquor (Source: Sixta, H. (2006). Handbook of Pulp. Weinheim: Wiley-VCH. Table 9.2.).
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 2.4800000000000026E-7 kg2.4800000000000026E-7 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 6.399999999999996E-6 kg6.399999999999996E-6 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to fresh water CA-QC 3.5276589172639935E-5 kg3.5276589172639935E-5 kg
General comment Effluent characterization measured at the factory.
Elementary flow
Emissions / Emissions to water / Emissions to fresh water CA-QC 1.4752028199467617E-4 kg1.4752028199467617E-4 kg
General comment Effluent characterization measured at the factory.
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 3.040000000000003E-4 kg3.040000000000003E-4 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 1.080000000000001E-8 kg1.080000000000001E-8 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to fresh water CA-QC 5.463714147950965E-5 kg5.463714147950965E-5 kg
General comment No data available for DOC. DOC=TOC as proposed by ecoinvent Data Quality Guidelines.
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 3.164000000000003E-4 kg3.164000000000003E-4 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 1.5240000000000015E-5 kg1.5240000000000015E-5 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 4.970792110690175E-5 kg4.970792110690175E-5 kg
General comment Effluent characterization measured at the factory.
Elementary flow
Emissions / Emissions to water / Emissions to fresh water CA-QC 5.463714147950965E-5 kg5.463714147950965E-5 kg
General comment No data available for TOC. TOC=COD/2.7 as proposed by ecoinvent Data Quality Guidelines.
Elementary flow
Emissions / Emissions to water / Emissions to fresh water CA-QC 0.012960939558293114 m30.012960939558293114 m3
General comment To river.
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified CA-QC 4.800000000000005E-8 kg4.800000000000005E-8 kg
General comment Amount estimated with emissions from the datasets "fluting medium production, semichemical, GLO 2008" and "treatment of recovered paper to fluting medium, wellenstoff, GLO 2008". The amount from these datasets were weighted according to the virgin and recycled fibre content (60% and 40% respectively).