| 关键数据集信息 | |
| 位置 | CN |
| 参考年 | 2019 |
| 名字 |
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| 数据集使用建议 | 该数据集来源于污染源普查报告，包含污染物排放及相关产品信息，但不包含能源或化学品消耗数据，也不提供废弃物或共生产物产生信息。在使用该数据集时，请根据实际情况补充缺失数据后再使用。 |
| 产品或过程的技术目的 | 该工业过程用于通过鲜牛奶发酵在各种规模上生产乳酸菌饮料。所描述的尾端处理技术用于管理废水污染，特别是去除氨氮、总磷、有机结合氮和化学需氧量（COD）。这项技术包括物理化学处理、厌氧生物处理、好氧生物处理，有时还包括物理处理，以实现高效率的污染物去除。 |
| 分类 |
类名
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层次结构级别
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| 关于数据集的一般性意见 | the Technical of end-of-pipe management technology for pollution chemical oxygen demandisPhysicochemical treatment + anaerobic biological treatment + aerobic biological treatment，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 = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours) |
| 版权 | 不 |
| 数据集的所有者 | |
| 参考定量 | |
| 参考流 |
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| 技术代表性 | |
| 技术说明，包括后台系统 | the Technical of end-of-pipe management technology for pollution chemical oxygen demandisPhysicochemical treatment + anaerobic biological treatment + aerobic biological treatment，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 = operating time of wastewater terminal treatment facilities (hours) / normal production time (hours) |
| 生命周期清单方法和分配 | |||||
| 数据集的类型 | Unit process, single operation | ||||
| 数据来源、处理和代表性 | |||||
| 偏离数据处理和外推原则/解释 | None | ||||
| 用于此数据集的数据源 | |||||
| 完整性 | |||||
| 产品模型的完整性 | No statement | ||||
| 验证 | |||||
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| 数据生成 | |
| 数据集生成/建模 | |
| 出版和所有权 | |
| UUID | 78fe2a0c-2905-4180-a753-6d12dc7c3659 |
| 最后修订日期 | 2024-04-15T22:07:06.859671+08:00 |
| 数据集版本 | 00.01.005 |
| 永久数据集 URI | https://lcadata.tiangong.world/showProcess.xhtml?uuid=78fe2a0c-2905-4180-a753-6d12dc7c3659&version=01.00.000&stock=TianGong |
| 数据集的所有者 | |
| 版权 | 不 |
| 许可证类型 | Free of charge for all users and uses |
输入
输出
| 流类型 | 分类 | 流 | 位置 | 平均量 | 计算量 | 最小量 | 最大量 | ||
|---|---|---|---|---|---|---|---|---|---|
| Product flow | Materials production / Organic chemicals | 1000.0 kg | 1000.0 kg | ||||||
| |||||||||
| 0.001928 | 0.001928 | ||||||||
| |||||||||
| 0.0024100000000000002 | 0.0024100000000000002 | ||||||||
| |||||||||
| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.0032480000000000005 kg | 0.0032480000000000005 kg | ||||||
| |||||||||
| 3640.0 | 3640.0 | ||||||||
| |||||||||
| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.004059999999999999 kg | 0.004059999999999999 kg | ||||||
| |||||||||
| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.009855000000000001 kg | 0.009855000000000001 kg | ||||||
| |||||||||
| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.01314 kg | 0.01314 kg | ||||||
| |||||||||
| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.06643 kg | 0.06643 kg | ||||||
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| Elementary flow | Emissions / Emissions to water / Emissions to water, unspecified | 0.19929 kg | 0.19929 kg | ||||||
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