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Process Data set: Salted squash ; Mustard, leafy vegetables, beans, onions and garlic, roots and tubers, squash heads ; Washing + pickling/salting + desalting + dehydration + soaking ; All sizes; NESPS2 (en) en zh

Key Data Set Information
Location CN
Reference year 2019
Name
Salted squash ; Mustard, leafy vegetables, beans, onions and garlic, roots and tubers, squash heads ; Washing + pickling/salting + desalting + dehydration + soaking ; 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 所述工业过程涉及各种腌制蔬菜的生产,包括咸榨菜、芥菜、叶菜、豆类、葱、大蒜、根茎和榨菜头。生产过程包括清洗、腌制/盐渍、脱盐、脱水和浸泡蔬菜,适合各种规模的消费和烹饪用途。此外,采用多种末端处理技术处理含有氨氮、化学需氧量(COD)和总磷的废水。这些处理包括化学混凝、好氧和厌氧生物处理、生物接触氧化、序批式反应器(SBR)和沉降分离,确保根据技术效率标准降低污染物水平。
Classification
Class name : Hierarchy level
  • ILCD: Reference Parameters / Materials production / Food and renewable raw materials
General comment on data set the Technical of end-of-pipe management technology for pollution chemical oxygen demandis/
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 chemical oxygen demandis/
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 99627a09-0d67-447c-a991-235edfb6f2e6
Date of last revision 2024-04-15T22:08:23.182375+08:00
Data set version 00.01.005
Permanent data set URI https://lcadata.tiangong.world/showProcess.xhtml?uuid=99627a09-0d67-447c-a991-235edfb6f2e6&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
Product flow
Materials production / Food and renewable raw materials 1000.0 kg1000.0 kg
General comment nan
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.198 kg0.198 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisAnaerobic biological treatment + aerobic biological treatment,Its Technical efficiency of end-of-pipe management60,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 0.2475 kg0.2475 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisChemical coagulation + aerobic biological treatment,Its Technical efficiency of end-of-pipe management50,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 0.2475 kg0.2475 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisChemical coagulation + bio-contact oxidation process,Its Technical efficiency of end-of-pipe management50,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 0.2475 kg0.2475 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisChemical coagulation + SBR,Its Technical efficiency of end-of-pipe management50,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))
0.3642 0.3642
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisAnaerobic biological treatment + aerobic biological treatment,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 /
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 0.4455 kg0.4455 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalisPrecipitation separation,Its Technical efficiency of end-of-pipe management10,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 0.495 kg0.495 kg
General comment the Technical of end-of-pipe management technology for pollution phosphorus, totalis/,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))
0.5463 0.5463
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisChemical coagulation + aerobic biological treatment,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 = opreating time of treatment facilities (hours) / normal production time (hours)
0.5463 0.5463
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisChemical coagulation + bio-contact oxidation process,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 /
0.5463 0.5463
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisChemical coagulation + SBR,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 /
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 1.02315 kg1.02315 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisAnaerobic biological treatment + aerobic biological treatment,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 = power consumption of equipment (kWh) / (equipment rated power (kW) × equipment operating time (hours))
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 1.70525 kg1.70525 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisChemical coagulation + bio-contact oxidation process,Its Technical efficiency of end-of-pipe management75,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 3.1374 kg3.1374 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisAnaerobic biological treatment + aerobic biological treatment,Its Technical efficiency of end-of-pipe management90
3.2778 3.2778
General comment the Technical of end-of-pipe management technology for pollution Ammonia NitrogenisPrecipitation separation,Its Technical efficiency of end-of-pipe management10
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 3.4105 kg3.4105 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisChemical coagulation + aerobic biological treatment,Its Technical efficiency of end-of-pipe management50,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 3.4105 kg3.4105 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisChemical coagulation + SBR,Its Technical efficiency of end-of-pipe management50,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))
3.642 3.642
General comment the Technical of end-of-pipe management technology for pollution Ammonia Nitrogenis/
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 4.7061 kg4.7061 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisChemical coagulation + aerobic biological treatment,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 = opreating time of treatment facilities (days) / normal production time (days)
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 4.7061 kg4.7061 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisChemical coagulation + bio-contact oxidation process,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 = opreating time of treatment facilities (days) / normal production time (days)
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 4.7061 kg4.7061 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisChemical coagulation + SBR,Its Technical efficiency of end-of-pipe management85
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 6.1389 kg6.1389 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundisPrecipitation separation,Its Technical efficiency of end-of-pipe management10,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 6.821 kg6.821 kg
General comment the Technical of end-of-pipe management technology for pollution Nitrogen, organic boundis/,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 25.0992 kg25.0992 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandisPrecipitation separation,Its Technical efficiency of end-of-pipe management20
Elementary flow
Emissions / Emissions to water / Emissions to water, unspecified 31.374000000000002 kg31.374000000000002 kg
General comment the Technical of end-of-pipe management technology for pollution chemical oxygen demandis/