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Process Data set: Steam/hot water/other ; Bituminous coal ; Pulverized coal furnace ; All sizes; NESPS2 (en) en zh

Key Data Set Information
Location CN
Reference year 2019
Name
Steam/hot water/other ; Bituminous coal ; Pulverized coal furnace ; All sizes; NESPS2
Use advice for data set This dataset is derived from the Pollution Source Census Report and contains information on pollution emissions and related products. However, it does not include data on energy or chemical consumption, nor does it provide information on waste or co-product generation. When utilizing this dataset, please supplement the missing data based on actual conditions before use
Technical purpose of product or process 该数据集代表了工业过程中使用的各种尾气治理技术，这些过程主要涉及燃烧煤粉化的烟煤以产生蒸汽、热水或其他形式的能量。这些技术适用于所有规模的运营，并专门设计用于减少二氧化硫、烟尘和氮氧化物的排放。数据集详细说明了不同污染物管理方法的技术效率，包括石灰石/石灰脱硫湿法过程、纳碱法、干湿电除尘、机械除尘和SNCR及SCR技术等用于处理氮氧化物。
Classification
Class name : Hierarchy level
  • ILCD: Reference Parameters / Energy carriers and technologies / Heat and steam
General comment on data set the Technical of end-of-pipe management technology for pollution sulfur dioxideisSpray drying process，Its Technical efficiency of end-of-pipe management70
Copyright No
Owner of data set
Quantitative reference
Reference flow(s)
Technological representativeness
Technology description including background system the Technical of end-of-pipe management technology for pollution sulfur dioxideisSpray drying process，Its Technical efficiency of end-of-pipe management70
LCI method and allocation
Type of data set Unit process, single operation
Data sources, treatment and representativeness
Deviation from data treatment and extrapolations principles / explanations None
Data source(s) used for this data set
Completeness
Completeness of product model No statement
Validation
Type of review
Dependent internal review
Reviewer name and institution
Data generator
Data set generator / modeller
Publication and ownership
UUID 1d66c569-b500-43fc-9123-b96026f8b9f2
Date of last revision 2024-04-15T22:03:50.847613+08:00
Data set version 00.01.005
Permanent data set URI https://lcadata.tiangong.world/showProcess.xhtml?uuid=1d66c569-b500-43fc-9123-b96026f8b9f2&version=01.00.000&stock=TianGong
Owner of data set
Copyright No
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
Product flow
Energy carriers and technologies / Lignite based fuels 1000.0 kg1000.0 kg
General comment nan

Outputs

Type of flow Classification Flow Location Mean amount Resulting amount Minimum amount Maximum amount
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.7559999999999999 kg0.7559999999999999 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSCR，Its Technical efficiency of end-of-pipe management80
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.7559999999999999 kg0.7559999999999999 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSNCR-SCR combination，Its Technical efficiency of end-of-pipe management80
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.944 kg0.944 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSCR，Its Technical efficiency of end-of-pipe management80
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.944 kg0.944 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSNCR-SCR combination，Its Technical efficiency of end-of-pipe management80
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 2.645999999999999 kg2.645999999999999 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSNCR，Its Technical efficiency of end-of-pipe management30
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 3.304 kg3.304 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSNCR，Its Technical efficiency of end-of-pipe management30
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 3.78 kg3.78 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesis/，Its Technical efficiency of end-of-pipe management0
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 4.72 kg4.72 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesis/，Its Technical efficiency of end-of-pipe management0
Product flow
Materials production / Inorganic chemicals 9187.0 m39187.0 m3
General comment the Technical of end-of-pipe management technology for pollution Exhaust gasis/
Product flow
Materials production / Inorganic chemicals 9187.0 m39187.0 m3
General comment the Technical of end-of-pipe management technology for pollution Exhaust gasisWith terminal treatment technology
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment Pollutant indicator sulfur dioxide end-of-pipe treatment technology is /, its efficiency is 0. The original document describes the pollutant category as exhaust gas, the pollutant indicator is sulfur dioxide, here to match it to the LCAflow library in the most compatible flow, the pollutant indicator note for sulfur dioxide original description of the production coefficient of 17S (no furnace desulfurization). Please modify the corresponding emissions after accounting for yourself according to the note.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment Pollutant indicator sulfur dioxide end-of-pipe treatment technology is /, its efficiency is 0. The original document describes the pollutant category as exhaust gas, the pollutant indicator is sulfur dioxide, here to match it to the LCAflow library in the most compatible flow, the pollutant indicator note for sulfur dioxide original description of the production coefficient of 13.6S (in-furnace desulfurization). Please modify the corresponding emissions after accounting for yourself according to the note.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment Pollutant indicators of sulfur dioxide end-of-pipe treatment technology is wet de-dusting method, the efficiency of which is 15, end-of-pipe treatment facilities actual operating rate (k value) calculation formula for K = desulfurization facilities annual operating hours / boiler annual operating hours. The original document describes the pollutant category as exhaust gas, pollutant indicators for sulfur dioxide, here to match it to the LCAflow library face to face the most compatible flow, pollutant indicators note for sulfur dioxide original description of the production coefficient of 17S (no furnace desulfurization). Please modify the corresponding emissions according to the note after self-calculation.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment The end-of-pipe treatment technology for the pollutant indicator soot is /, and its efficiency is 0. The original document describes the pollutant category as exhaust gas, and the pollutant indicator as soot, and the matching work is carried out here to match it to the flow that is most compatible with the LCAflow library, and the production coefficient of the pollutant indicator, which is described in the original document as soot, is 8.93 A. Please modify the corresponding emission level after accounting according to the notes..The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisBag filter technology，Its Technical efficiency of end-of-pipe management99.6.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisDry electrostatic precipitation technology，Its Technical efficiency of end-of-pipe management97.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisElectric-bag composite precipitator，Its Technical efficiency of end-of-pipe management99.8.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisMechanical dust removal + wet precipitation and desulfurization，Its Technical efficiency of end-of-pipe management92.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisMechanical dust removal + wet precipitation，Its Technical efficiency of end-of-pipe management92.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Product flow
Wastes / Production residues 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution Flue dustisWet electrostatic precipitation，Its Technical efficiency of end-of-pipe management70.The original article describes the pollution production coefficients as 8.93A。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 8.93A. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisAmmonia method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisAmmonia method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDouble alkali process，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDouble alkali process，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisFlue gas circulating fluidized bed method，Its Technical efficiency of end-of-pipe management85.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisFlue gas circulating fluidized bed method，Its Technical efficiency of end-of-pipe management85.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisLimestone/lime-gypsum wet process，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisLimestone/lime-gypsum wet process，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisMagnesium oxide method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisMagnesium oxide method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisSodium alkali method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisSodium alkali method，Its Technical efficiency of end-of-pipe management92.5.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisSpray drying process，Its Technical efficiency of end-of-pipe management70.The original article describes the pollution production coefficients as 17S（无炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 17S（无炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0 kg0.0 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisSpray drying process，Its Technical efficiency of end-of-pipe management70.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）。Please revise the corresponding emissions after accounting for them according to the notes.。.The original article describes the pollution production coefficients as 13.6S（炉内脱硫）. Please revise the corresponding emissions after accounting for them according to the notes.