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Process Data set: Dicamba ; Synthesis ; All sizes; NESPS2 (en) en zh

Key Data Set Information
Location CN
Reference year 2019
Name
Dicamba ; Synthesis ; 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 本技术过程包括在所有规模上合成除草剂二甲苯氧乙酸(dicamba)(2,5-二氯苯氧乙酸)。尾气处理管理技术包括电解,氧化还原过程,成型厌氧反应器,A/O过程,化学絮凝以及RTO(再生热氧化)系统。这些是工业过程和技术,用于处理像化学需氧量(COD)、氮、有机化合物、废气和挥发性有机化合物(VOCs)这样的dicamba生产废物流。
Classification
Class name : Hierarchy level
  • ILCD: Reference Parameters / Materials production / Organic chemicals
General comment on data set the Technical of end-of-pipe management technology for pollution Exhaust gasis/,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 = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
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 Exhaust gasis/,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 = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment 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 b2f04cdd-c4e9-4810-b000-488a51f7147d
Date of last revision 2024-04-15T22:09:25.741759+08:00
Data set version 00.01.005
Permanent data set URI https://lcadata.tiangong.world/showProcess.xhtml?uuid=b2f04cdd-c4e9-4810-b000-488a51f7147d&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 0.2759999999999843 kg0.2759999999999843 kg
General comment the Technical of end-of-pipe management technology for pollution volatile organic compoundisRTO,Its Technical efficiency of end-of-pipe management99.9,The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Product flow
Materials production / Organic chemicals 1000.0 kg1000.0 kg
General comment nan
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 8.28 kg8.28 kg
General comment the Technical of end-of-pipe management technology for pollution volatile organic compoundis(Absorption + diversion) + (adsorption + steam desorption)/(adsorption + nitrogen/air desorption),Its Technical efficiency of end-of-pipe management97,The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.0669 kg0.0669 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisElectrolysis + redox process + shaped anaerobic reactor + A/O process + chemical coagulation,Its Technical efficiency of end-of-pipe management97,The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.223 kg0.223 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisShaped anaerobic reactor + A/O process,Its Technical efficiency of end-of-pipe management90,The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 4.04 kg4.04 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisElectrolysis + redox process + shaped anaerobic reactor + A/O process + chemical coagulation,Its Technical efficiency of end-of-pipe management98,The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is k = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Product flow
Materials production / Inorganic chemicals 10000.0 m310000.0 m3
General comment the Technical of end-of-pipe management technology for pollution Exhaust gasis/,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 = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))