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混凝与絮凝设计

分类烧杯试验剂量重复数据,进行有界筛选插值、快速混合池容积与功率估算,以及絮凝水力计算。

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PROJECT · OPTIONAL

Project metadata

Optional report context; it does not change calculations.Edit detailsHide details

01 · USER INPUT

Design basis and inputs

Rapid Mix design mode

Choose one hydraulic basis. Volume and detention are reconciled from this mode and design flow.

Jar-Test criterion

Jar-Test Observations

Enter each replicate separately. A dose level passes only when every replicate passes.

Dose (mg/L)ResponseReplicate ID optionalRow action

Flocculation Stages

Each stage uses design flow and one declared sizing mode.

StageModeDetention time or volumeG (s⁻¹)Row action
Must be greater than 0.Must be greater than 0.
Must be greater than 0.Must be greater than 0.
Calculations run locally in this browser. No input data is sent to an API.

02 · CALCULATED RESULT

Engineering Results

Enter the design basis and observations, then calculate to create a result.

03 · REPORTING

Exports and verification

PDF includes current report metadata. Engineering input changes mark results stale and disable all exports.

Verification suite

Calculation revision 1.1

80 focused fixtures: replicate classification and order invariance, criterion validation, signed responses, conservative interpolation, hydraulic sizing and checks, export state, and invalid-input rejection. 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

依据声明的判据分类烧杯试验重复样,并根据输入流量、几何尺寸、黏度和运行判据筛选快速混合与絮凝的体积、停留时间、G 值及液体功率。计算的混合功率是液体耗散功率,不是电机、轴、传动装置或电气铭牌功率。

Each jar-test observation is classified independently. A dose level is confirmed PASS only when all valid replicates pass; mixed dose levels do not qualify. Replicate responses are not averaged.

Threshold interpolation is linear and bounded to adjacent unique tested dose levels. A replicated dose in a crossing bracket makes interpolation unavailable. Extrapolation is not performed.

Within-range and explicit criteria report dose-level classifications without a single interpolated dose.

Rapid-mix sizing uses V = Q × t or, for an existing basin, t = V / Q. The same physical volume is used for hydraulics and calculated liquid mixing power P = μVG². Gt = G × t.

Each flocculation stage uses either V = Q × t or t = V / Q. Calculated liquid mixing power is P = μVG² and stage Gt = G × t. The sum of stage G×t contributions is descriptive and is not asserted as a universal criterion.

Optional alkalinity demand is the user-entered factor multiplied by the lowest confirmed tested passing dose.

范围 / 限制

  • 依据用户声明的烧杯试验判据和水质参数,审查已测试剂量、快速混合容积与功率,以及分段絮凝停留时间和 G×t。
  • Does not select a coagulant, predict finished turbidity, predict pH from first principles, or guarantee full-scale performance.
  • A screening interpolation is not a tested dose and is never substituted for the confirmed tested dose in alkalinity demand.
  • No universal optimum G or Gt is asserted. Dynamic viscosity has no hidden temperature assumption.
  • Calculated liquid mixing power is the power dissipated in the liquid implied by entered G, viscosity, and volume. It is not motor, shaft, drive, or electrical nameplate power; equipment selection requires mechanical and drive efficiency and equipment-specific design factors.
02

工程路径

上游背景

当前工具决策

  • 混凝与絮凝设计 分类烧杯试验剂量重复数据,进行有界筛选插值、快速混合池容积与功率估算,以及絮凝水力计算。

下游工程步骤

  • 沉淀池设计 根据项目依据比较澄清、气浮或过滤等备选方案;不预设唯一分离工艺。
  • 溶气气浮(DAF)设计 根据项目依据比较澄清、气浮或过滤等备选方案;不预设唯一分离工艺。
  • 粒状滤料过滤器设计 根据项目依据比较澄清、气浮或过滤等备选方案;不预设唯一分离工艺。