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Process Data set: Glyphosate ; Diethanolamine, phosphite, paraformaldehyde ; IDA method - diethanolamine redox bis(glyphosate) process + glyphosate synthesis ; All sizes; NESPS2 (en) en zh

Key Data Set Information
Location CN
Reference year 2019
Name
Glyphosate ; Diethanolamine, phosphite, paraformaldehyde ; IDA method - diethanolamine redox bis(glyphosate) process + glyphosate 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 本工业过程涉及草甘膦的生产和合成，这是一种广泛用于农业中控制广谱杂草的除草剂配方。该工业规模生产包括适用于所有规模草甘膦合成的IDA方法——二乙醇胺氧化还原双甘膦工艺等过程。此外，用于污染控制的末端处理技术与处理这些工业过程产生的废水有关。
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 phosphorus, totalisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，Its Technical efficiency of end-of-pipe management52
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 phosphorus, totalisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，Its Technical efficiency of end-of-pipe management52
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 ac69f526-1d86-4373-8348-cb749796187a
Date of last revision 2024-04-15T22:09:13.499391+08:00
Data set version 00.01.005
Permanent data set URI https://lcadata.tiangong.world/showProcess.xhtml?uuid=ac69f526-1d86-4373-8348-cb749796187a&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
7.099999999999597E-4 7.099999999999597E-4
General comment the Technical of end-of-pipe management technology for pollution Ammonia Nitrogenis(2500 others) Incineration，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 = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual 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 2.06 kg2.06 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) + photocatalysis，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 /
Elementary flow
Emissions / Emissions to air / Emissions to air, unspecified 3.09 kg3.09 kg
General comment the Technical of end-of-pipe management technology for pollution volatile organic compoundisCondensation + (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 /
0.0070999999999999995 0.0070999999999999995
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，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))
8000.0 8000.0
General comment the Technical of end-of-pipe management technology for pollution Waste wateris/，Its Technical efficiency of end-of-pipe management0
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.0123999999999993 kg0.0123999999999993 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundis(2500 others) Incineration，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 = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
0.014199999999999999 0.014199999999999999
General comment the Technical of end-of-pipe management technology for pollution Ammonia Nitrogenis(1700 others) Deamination tower + chemical precipitation + A2/O process，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 = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
0.028399999999999998 0.028399999999999998
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisShaped anaerobic reactor + biological filter + chemical coagulation + redox process + biofilm process，Its Technical efficiency of end-of-pipe management96
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.052199999999997033 kg0.052199999999997033 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalis(2500 others) Incineration，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 /
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.16699999999999052 kg0.16699999999999052 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandis(2500 others) Incineration，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 = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.6680000000000095 kg0.6680000000000095 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisShaped anaerobic reactor + biological filter + chemical coagulation + redox process + biofilm process，Its Technical efficiency of end-of-pipe management99.6，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 water / Emissions to water, unspecified 0.868 kg0.868 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，Its Technical efficiency of end-of-pipe management93，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 water / Emissions to water, unspecified 1.24 kg1.24 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisShaped anaerobic reactor + biological filter + chemical coagulation + redox process + biofilm 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 = annual power consumption of wastewater treatment facilities (kWh) / (total rated power (kW) × annual operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 1.67 kg1.67 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，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 = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours)
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 2.604 kg2.604 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundis(1700 others) Deamination tower + chemical precipitation + A2/O，Its Technical efficiency of end-of-pipe management79，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 water / Emissions to water, unspecified 8.874 kg8.874 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisShaped anaerobic reactor + biological filter + chemical coagulation，Its Technical efficiency of end-of-pipe management83，The formula for calculating the actual operation rate (k-value) of the end-of-pipe treatment facility is /
Product flow
Materials production / Inorganic chemicals 9830.0 m39830.0 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 /
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 10.962 kg10.962 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalis(1700 others) Deamination tower + chemical precipitation + A2/O process，Its Technical efficiency of end-of-pipe management79，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 water / Emissions to water, unspecified 11.69 kg11.69 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandis(1700 others) Deamination tower + chemical precipitation + A2/O process，Its Technical efficiency of end-of-pipe management93，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 water / Emissions to water, unspecified 25.056 kg25.056 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisRedox process + shaped anaerobic reactor + activated sludge process + A/O process，Its Technical efficiency of end-of-pipe management52