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エンジニアリングツール · 水処理

排水前処理設計ツール

明示されたプロジェクト・メーカー資料を用いて、流量ケース、水路水理、スクリーン・除砂設備の定格能力、冗長性、および任意の残渣処理量を確認します。

状態
公開中

ENGINEERING WORKBENCH · STAGE 02

Headworks process train

Manual, explicit influent flow cases. No hidden browser-state import.

  1. 01HEADWORKS INFLUENT
  2. 02SCREENING
  3. 03GRIT REMOVAL
  4. 04PRETREATED INFLUENT

Workflow path Influent / Acceptance → Preliminary Treatment → Equalization where required (optional) → Primary Treatment. Equalization remains conditional on declared variability; values transfer manually.

01 · PROJECT AND FLOW BASIS

Headworks design inputs

The peak-hour input is entered as a flow rate for one hour. Required hierarchy checks enforce Minimum ≤ Average Day ≤ Maximum Day and Peak Hour ≥ Average Day. Peak Hour below Maximum Day is a basis-review warning only; event flow is outside this hierarchy.

Required flow cases

Each flow includes source provenance.

Bounded event / shock flow

Optional · requires a positive duration and source

02 · SCREEN / CHANNEL EQUIPMENT

Installed and duty basis

Screen equipment ratings and channel hydraulics use separate counts. Each channel is modeled with the same entered width and operating depth, with equal flow split across channels in service.

03 · SCREENING DESIGN

Opening area, velocity criteria, and headloss basis

Technology boundaryRepeated-bar geometry is available only for coarse/fine bar racks. Perforated plate, step, drum, and proprietary screens require vendor/project effective area or rated capacity. The EPA equation below is limited to a clean bar screen.

Effective open area

Geometry dimensions are projected normal to through-flow.

Project velocity criteria

Calculated values are reported separately from declared criteria.

Screen headloss

Basis and flow point stay visible in results and exports.
EPA clean bar-screen methodhL = (V² − v²) / (2 × 0.7 × g)V = velocity through bar openings; v = approach velocity. Clean bar screens only. Fouled loss is not inferred.

04 · CHANNEL HYDRAULICS

Minimum and design-flow channel checks

Approach velocity uses Q divided by the gross wetted area of the entered number of channels in service. Through-screen velocity uses effective opening area when the selected method supports it. Screen equipment capacity is evaluated from its separate duty count.

Velocity across explicit flow cases

Flow caseTotal flowApproach velocityThrough-screen velocityCalculated / rated lossHeadloss basis / provenanceDuty utilization
Calculate to populate these values.
Capacity by flow case is available after calculation.

05 · GRIT REMOVAL

Technology-specific hydraulic and equipment basis

Horizontal-flow chamber velocity criteria are project inputs. Aerated and vortex/proprietary capacity is vendor/project-rated. No generic capture efficiency is predicted.

Geometry and hydraulic detention

Required rectangular active-channel geometry.

Optional declared performance basis

Never labeled as an ATLAS prediction.

06 · REDUNDANCY AND FAILURE CASES

Selected one-unit-out capacity and hydraulics

Failure scenarios use separate screen and channel counts: one screen out, one channel out, a paired screen-and-channel N−1 case, and all installed screens/channels. Vendor headloss curves are not extrapolated for failure cases.

Screen duty and failure-case checks

ScenarioAvailable screensActive channelsHydraulic capacityUtilizationCapacity marginActual shortfallApproach velocityThrough-screen velocityHeadlossHeadloss method / basis
Calculate to populate these values.

07 · OPTIONAL HANDLING BASIS

Screenings and grit quantities

Solids identity: influent TSS is not screenings and is not grit. Screenings and grit are separate from primary sludge and biological sludge. Quantities below require a declared measured/project/vendor rate.

Screenings handling basis

Grit handling basis

08 · DETAILED RESULTS

Engineering values and limitations

Calculate a valid input snapshot to populate detailed results. Infeasible inputs do not expose a normal design result.

Revision ww-headworks-1.1.0 · deterministic local calculation · explicit project/vendor assumptions

Vendor-rated screen/grit performance must be verified for the selected equipment. Generic hydraulic screening does not predict proprietary capture efficiency. Influent TSS is not screenings production and is not grit production. This preliminary check does not replace equipment supplier hydraulic curves or detailed civil/mechanical design.

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

明示されたプロジェクト・メーカー資料を用いて、流量ケース、水路水理、スクリーン・除砂設備の定格能力、冗長性、および任意の残渣処理量を確認します。

前提

  • 前処理を統合したワークベンチです。専有設備の捕捉率や流入 TSS からスクリーンかす・砂量を予測せず、メーカー曲線や詳細な土木・機械設計の代替にはなりません。

範囲 / 制限事項

  • 前処理を統合したワークベンチです。専有設備の捕捉率や流入 TSS からスクリーンかす・砂量を予測せず、メーカー曲線や詳細な土木・機械設計の代替にはなりません。
02

エンジニアリングパス

上流の前提

  • 廃水流入水の設計基準 前処理を統合したワークベンチです。専有設備の捕捉率や流入 TSS からスクリーンかす・砂量を予測せず、メーカー曲線や詳細な土木・機械設計の代替にはなりません。

このツールでの設計判断

  • 排水前処理設計ツール 明示されたプロジェクト・メーカー資料を用いて、流量ケース、水路水理、スクリーン・除砂設備の定格能力、冗長性、および任意の残渣処理量を確認します。

下流の設計ステップ

  • 排水均等化槽設計ツール 入力した流入量と制御流出量の時系列から有効貯留量と運転時の貯留量を評価します。 任意:申告された流量変動が均等化を必要とする場合に使用します。値は手動入力で、自動転送はありません。
  • 沈殿池設計 前処理を統合したワークベンチです。専有設備の捕捉率や流入 TSS からスクリーンかす・砂量を予測せず、メーカー曲線や詳細な土木・機械設計の代替にはなりません。