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粒状滤料过滤器设计

审查正常和单格停运时的滤速、多层滤料水头损失及反冲洗用水需求。

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PROJECT · OPTIONAL

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Report context for exports; it does not change calculations.Edit detailsHide details

01 · USER INPUT

Design basis and inputs

Enter each layer's volume-equivalent spherical particle diameter and separate sphericity. If a supplier gives an already shape-corrected surface-volume diameter, divide it by sphericity before entry.

Sand
Sand
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02 · CALCULATED RESULT

Results at a glance

Load or enter inputs, then calculate to create an authoritative result.

03 · REPORTING

Exports and verification

CSV contains input and output detail. PDF uses the current calculation and report metadata.

Verification suite

Calculation revision 4f9f386b

66 focused fixtures: independent filter-bank, backwash, and multilayer Ergun cases; selected headloss basis, optional expansion, finite-result boundaries, validation, and structured reporting. Tests are deterministic and run without network access.

此工程工具目前仅提供英文版本。

01

工程依据

方法

根据输入的滤料和水性质计算正常及少一格滤池工况的负荷、反冲洗流量/水量和清洁床分层 Ergun 水头损失。颗粒直径应输入体积等效球形直径,并单独应用球形度;Ergun 结果仅为清洁床筛选值。

Normal rate = plant design flow / total active filter area. One-filter-out rate uses (N−1) equal filter areas. Rates are reported in m/d and m/h.

Backwash flow = backwash rate × area per filter. Wash volume = flow × duration. Daily volume includes entered washes per filter per day.

Backwash-water fraction = gross daily backwash-water volume / entered plant design flow; it does not represent net recovery.

Clean-bed headloss uses the Ergun equation for each entered layer and sums the layer losses. Enter the volume-equivalent spherical particle diameter; sphericity is applied separately. Velocity converts m/h to m/s; pressure drop converts to head using entered density and standard gravitational acceleration.

A declared bed expansion is applied to layer depth for a geometric screen only. Leaving it blank omits that screen.

范围 / 限制

  • 依据声明的滤料特性、反冲洗强度和持续时间,以及可选的滤床膨胀率,对比正常、N−1 或自定义水头损失工况。
  • Does not recommend media chemistry, predict terminal run time from turbidity, predict pathogen removal, or claim regulatory filter credit.
  • Ergun output is a clean-bed screening estimate. Volume-equivalent spherical diameter, porosity, sphericity, and water properties must be supplied explicitly; do not enter an already shape-corrected surface-volume diameter without converting it first.
  • Bed expansion is not predicted from wash hydraulics.
02

工程路径

上游背景

  • 已选上游固体控制依据 应用所选滤料或深度屏障筛选前,先确认进水水质与固体控制假设。

当前工具决策

  • 粒状滤料过滤器设计 审查正常和单格停运时的滤速、多层滤料水头损失及反冲洗用水需求。

下游工程步骤