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OxyMatrix 曝气与氧传质工程

评估生物处理需氧量、氧传质性能、曝气器供气量和鼓风机选型,为污水曝气系统初步设计提供依据。

状态
可用
单位
公制 / 英制显示
Calculation serviceUnavailable
Engineering resultNot available

Automatic calculation · preliminary design

计算模式

1. Biological Process & Oxygen Demands

Carbonaceous demand, nitrification stoichiometry & denitrification credit

Stage 1 /
Qm³/d
°C
mg/L
Target
mg/L
Biological Screening AssumptionsUse project/site-specific values where available.
g VSS/g BOD₅
Per gram of removed
Factor
mg/L
Target
mg/L
mg/L
By denitrification · oxygen credit
mg/L
PF
Peak oxygen-demand multiplier
mg/L

2. Submerged Physics & Reference Transfer

Diffuser submergence, pressure screening, and standard oxygen requirement

Stage 2 /
Hm
Hᵈm
fₑ
Effective depth = fraction × basin liquid depth
zm
Above sea level
Depth Slope
%/m
Per metre of diffuser submergence
α
Process-water correction
β
Dissolved-oxygen saturation correction
F
Diffuser fouling allowance
θ
Temperature correction for transfer kinetics
ΔPᵈkPa
ΔPₚkPa

3. Blower Thermodynamics & Sizing

Compression technology, isentropic efficiency, and wire power

Stage 3 / Power

Selecting a technology loads its reference screening efficiency into the editable current design fields.

°C
°C
%
Technology Reference82%
Current Design75%
Modified from reference
%
Technology reference: 82%
%
Editable design input
%
Editable design input
CAD/kWh
h/yr
Calculation service unavailableNo result is available because the calculation service could not be reached. Your inputs remain available.

Submerged Aeration Tank — Design Schematic

Submergence, pressure and oxygen-transfer context

Unavailable
No diagram resultThe calculation service is unavailable; the diagram will appear after a successful response.
Reference-based preliminary design. Review engineering assumptions and limitations in Derivations.

此工程工具目前仅提供英文版本。

01

工程依据

方法

关联生物处理需氧量、浸没式曝气和鼓风机选型,提供氧传质、需气量、曝气器布置、鼓风机性能及能耗评估。

假设

  • 结合工艺条件校核 α 系数、β 系数、标准氧转移效率(SOTE)、溶解氧(DO)、曝气器淹没水深和场地海拔。

范围 / 限制

  • 基于参考资料的初步评估与设计。详细设计须经项目工程复核,并采用供应商性能数据;结果不构成设计认证、供应商性能保证或监管批准。
02

工程路径

生物 AOR 来源(二选一)

氧传递设计

  • OxyMatrix 使用已接受的 AOR,并负责传质、风量、曝气器、鼓风机和能耗计算。

下游支持

  • 曝气设备 / 下游生物工艺支持 使用 OxyMatrix 结果支持曝气设备选型和下游生物工艺设计。