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Process Data set: Coke oven ; Coke ; Coking coal ; Top loading ; Carbonization chamber greater than or equal to6m; NESPS2 (en) en zh

Key Data Set Information
Location CN
Reference year 2019
Name
Coke oven ; Coke ; Coking coal ; Top loading ; Carbonization chamber greater than or equal to6m; 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 所描述的工业过程是一种使用顶装炭化室（高度大于或等于6米）的焦炭生产方法。这个过程主要应用于冶金行业，从炼焦煤中生产焦炭，这是铁和钢制造不可或缺的材料。提到的管道末端管理技术用于控制焦化过程中的颗粒物（PM2.5 - PM10）、二氧化硫、挥发性有机化合物（VOCs）和氮氧化物（NOx）的排放。这些技术对于满足环境法规和减少污染对空气质量影响至关重要。
Classification
Class name : Hierarchy level
  • ILCD: Reference Parameters / Energy carriers and technologies / Hard coal based fuels
General comment on data set the treatment technology for the pollution of Exhaust gasdidn't offered，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Copyright No
Owner of data set
Quantitative reference
Reference flow(s)
  • - 1000.0 * 1.0 kg (Mass)
Technological representativeness
Technology description including background system the treatment technology for the pollution of Exhaust gasdidn't offered，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
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 5f0051ab-5c18-4335-81d4-0f8f59793867
Date of last revision 2024-04-15T22:05:58.715557+08:00
Data set version 00.01.005
Permanent data set URI https://lcadata.tiangong.world/showProcess.xhtml?uuid=5f0051ab-5c18-4335-81d4-0f8f59793867&version=01.00.000&stock=TianGong
Owner of data set
Copyright No
License type Free of charge for all users and uses

Inputs

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 3.2E-5 kg3.2E-5 kg
General comment the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isBag filter，Its Technical efficiency of end-of-pipe management99
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 2.45E-4 kg2.45E-4 kg
General comment the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isBag filter，Its Technical efficiency of end-of-pipe management99，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 6.949999999999999E-4 kg6.949999999999999E-4 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisAmmonia method，Its Technical efficiency of end-of-pipe management95
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 6.949999999999999E-4 kg6.949999999999999E-4 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDouble alkali process，Its Technical efficiency of end-of-pipe management95
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0014 kg0.0014 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisLimestone/gypsum method, lime/gypsum method，Its Technical efficiency of end-of-pipe management90
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.002115 kg0.002115 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisRotary spray drying method，Its Technical efficiency of end-of-pipe management85
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.00213 kg0.00213 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisOthers (dry desulfurization)，Its Technical efficiency of end-of-pipe management85，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0032 kg0.0032 kg
General comment the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isDirect discharge，Its Technical efficiency of end-of-pipe management0，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0046 kg0.0046 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisAmmonia method，Its Technical efficiency of end-of-pipe management95
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0046 kg0.0046 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDouble alkali process，Its Technical efficiency of end-of-pipe management95
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0092 kg0.0092 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisLimestone/gypsum method, lime/gypsum method，Its Technical efficiency of end-of-pipe management90
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0138 kg0.0138 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisOthers (dry desulfurization)，Its Technical efficiency of end-of-pipe management85
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0138 kg0.0138 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisRotary spray drying method，Its Technical efficiency of end-of-pipe management85
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0139 kg0.0139 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDirect discharge，Its Technical efficiency of end-of-pipe management0
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0203 kg0.0203 kg
General comment the Technical of end-of-pipe management technology for pollution volatile organic compoundisDirect discharge，Its Technical efficiency of end-of-pipe management0，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.0245 kg0.0245 kg
General comment the Technical of end-of-pipe management technology for pollution particles (PM2.5 - PM10)isDirect discharge，Its Technical efficiency of end-of-pipe management0，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.03975 kg0.03975 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSCR，Its Technical efficiency of end-of-pipe management85，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.07185 kg0.07185 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisSCR，Its Technical efficiency of end-of-pipe management85，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.092 kg0.092 kg
General comment the Technical of end-of-pipe management technology for pollution sulfur dioxideisDirect discharge，Its Technical efficiency of end-of-pipe management0
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.265 kg0.265 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisDirect discharge，Its Technical efficiency of end-of-pipe management0，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 0.479 kg0.479 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen oxidesisDirect discharge，Its Technical efficiency of end-of-pipe management0，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Product flow
Energy carriers and technologies / Hard coal based fuels 1000.0 kg1000.0 kg
General comment nan
Product flow
Materials production / Inorganic chemicals 1280.0 m31280.0 m3
General comment the treatment technology for the pollution of Exhaust gasdidn't offered，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Product flow
Materials production / Inorganic chemicals 1830.0 m31830.0 m3
General comment the treatment technology for the pollution of Exhaust gasdidn't offered，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))