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冷却塔水平衡与 LSI 计算器

计算冷却塔的蒸发、风吹、排污与补水量平衡,并通过朗格利尔饱和指数模型动态预警循环水的结垢与腐蚀风险。

状态
实时工程工具
模式
水量平衡 / LSI / RSI
工况
补充水 / 循环水
单位
公制 / 英制
ATLAS WTS · Process Engineering

Cooling Tower Water Balance & LSI Calculator

Evaporation, drift, blowdown and makeup water balance from mass conservation, plus Langelier Saturation Index scaling/corrosion risk screening for the circulating water.

Local Engine
Project Information
Heat Load & Water Balance

Cooling range (ΔT): —

Typical operating range: 3–6.

Default 0.00153 (metric, m³/h & °C basis) — see methodology note below. Typical range 0.00115–0.00195 for climate variation.

Circulating Water Chemistry (for LSI)
Estimate from Makeup Water Optional

If you only have makeup water lab data on hand, enter it here and estimate the concentrated circulating-water values (Ca, Alkalinity, TDS all scale × CoC at steady state). Note: pH does not scale linearly with CoC (CO2 stripping in the tower shifts the carbonate equilibrium) — estimated circulating pH typically settles between 8.2–8.8 unless acid is dosed. Enter your own circulating water pH reading above rather than scaling it.

Water Balance Results
Evaporation Loss (E)
—m³/h
E = k × Flow × ΔT
Drift Loss (D)
—m³/h
—
Blowdown Required (B)
—m³/h
B = E/(CoC−1) − D
Total Makeup Water (M)
—m³/h
M = E + D + B

Achieved CoC: —

Heat rejected (informational): —

Scaling & Corrosion Risk (LSI)
ℹ
—
Enter circulating water chemistry to evaluate scaling/corrosion risk.
Saturation pH (pHs)
—
Langelier Saturation Index
—
LSI = pH − pHs
Ryznar Stability Index
—
RSI = 2×pHs − pH
Design Notes & Warnings

Export includes the current water balance and water chemistry configuration and results.

Evaporation coefficient: the commonly cited "0.0008/0.00085 × flow × range" rule of thumb is an imperial constant (gpm, °F) — used directly against a Celsius ΔT without the required ×1.8 unit conversion it understates evaporation by roughly 1.8×. This tool defaults to the converted metric constant, 0.00153, cross-checked against the independent "~1% evaporation per 5.6°C range" industry rule of thumb.

此工程工具目前仅提供英文版本。

01

工程依据

方法

蒸发、风吹与排污遵循标准的质量守恒水平衡关系(CTI/ASHRAE 惯例):蒸发损失与循环水量 x 冷却温差成正比,风吹损失取决于所选除雾器性能等级,强制排污量则直接由稳态浓缩倍数质量守恒方程求解。

结垢/腐蚀倾向采用朗格利尔饱和指数(Langelier, 1936)计算,基于水温、pH、钙硬度、总碱度与 TDS,并纳入瑞兹纳稳定指数作为二次校核 —— 两者均为经验性筛查指标,不能替代完整的水处理药剂方案。

标准 / 参考依据

Langelier (1936)CTI / ASHRAE mass-balanceVendor-neutral

范围 / 限制

  • LSI 和 RSI 是经验筛查指标,不能替代完整的水处理药剂方案。
  • 基于 CTI/ASHRAE 质量守恒水平衡;采用朗格利尔(1936)饱和指数与瑞兹纳稳定指数进行厂家中立的结垢/腐蚀风险筛查。
02

工程路径

应用

场景

工作流