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エンジニアリングツール · 水処理

粒状ろ過材フィルター設計

通常時と1池停止時の負荷、多層ろ材の損失水頭、逆洗水量を確認します。

状態
公開中
PROJECT · OPTIONAL

Project metadata

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.

このエンジニアリングツールは現在、英語版のみ提供しています。

01

エンジニアリングの根拠

方法

入力されたろ材と水の特性から、通常時・1池停止時の負荷、逆洗流量/水量、多層清浄床の Ergun 損失を計算します。粒径は体積等価球径を入力し、球形度は別途適用します。Ergun の結果は清浄床のスクリーニング値です。

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.

範囲 / 制限事項

  • 指定されたろ材特性、逆洗流量と時間、任意の層膨張率に基づき、通常、N−1、またはユーザー定義の損失水頭条件を比較します。
  • 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

エンジニアリングパス

上流の前提

  • 選定された上流固形物管理の基準 ろ材または高度処理バリアを評価する前に、供給水と固形物管理の前提を確認します。

このツールでの設計判断

  • 粒状ろ過材フィルター設計 通常時と1池停止時の負荷、多層ろ材の損失水頭、逆洗水量を確認します。

下流の設計ステップ