Civil Engineering / Jar Test Coagulation
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LABORATORY 33 · CIVIL ENGINEERING

Jar Test Coagulation lab report

A worked jar test coagulation lab report with sample observation tables, regression plots, calculations, and error analysis.

WORKED EXAMPLE · BENCHMARK OBSERVATIONS

A complete example civil engineering laboratory report.

Simulated demonstration data.

This report illustrates formal civil engineering data reduction, instrument calibration tares, and structural parameter estimation. Replace its observations with your own experimental telemetry when preparing a civil engineering laboratory report submission.

Student: __________________Student ID: __________________Course: __________________Date: __________________Partner: __________________Instructor: __________________

1. Title and aim

Coagulation-Flocculation Optimization & Residual Turbidity via Standard Jar Test. Determine the optimum coagulant dosage (alum / polyaluminum chloride) and rapid/slow mixing conditions for maximum turbidity and suspended colloidal particle removal from raw surface water according to ASTM D2035.

2. Abstract

Six controlled civil engineering laboratory observations were systematically evaluated across operational settings Alum Dose D = 10.0 mg/L to Alum Dose D = 35.0 mg/L for Coagulation-Flocculation Optimization & Residual Turbidity via Standard Jar Test. Ordinary least-squares regression yielded an empirical Turbidity Removal Rate per Unit Coagulant of 0.8500 NTU/(mg/L) (difference from theoretical reference = 0.0000%). The empirical telemetry conclusively validates the fundamental civil engineering continuum and constitutive formulation with R² = 1.000000. The investigation demonstrates stable structural and physical behavior, measurement reproducibility, and strict adherence to international ASTM, AASHTO, and ISO standards.

3. Apparatus and fixed settings

4. Theory and graph choice

In civil environmental water treatment engineering, raw surface waters from rivers and reservoirs contain suspended silt, clay, pathogenic microorganisms, and natural organic matter (NOM) present as negatively charged microscopic colloids (0.001 to 1.0 µm). Due to electrostatic repulsion governed by negative zeta potentials (-15 to -30 mV), colloidal particles remain indefinitely suspended in stable Brownian motion and cannot settle by gravity alone. Coagulation and flocculation destabilize this colloidal suspension. Developed in the 1920s, the standard Jar Test (ASTM D2035) uses a multi-paddle stirrer to optimize chemical dosing in municipal water treatment plants. Adding hydrolyzing metal coagulants—such as aluminum sulfate (alum, Al₂(SO₄)₃·14H₂O) or ferric chloride (FeCl₃)—destabilizes colloids through two primary mechanisms: (1) Charge neutralization: trivalent cations (Al³⁺, Al(OH)²⁺, Al₇(OH)₁₇⁴⁺) compress the electrical diffuse double layer and neutralize negative surface charges; and (2) Sweep flocculation: at higher dosages and neutral pH (6.5 to 7.5), amorphous aluminum hydroxide Al(OH)₃ precipitates en masse, physically entrapping and sweeping suspended particles into settleable flocs. In this laboratory experiment, six 1-liter water samples are dosed with alum from 10 to 40 mg/L, subjected to 1-minute rapid mixing (100 rpm), 20-minute slow flocculation (30 rpm), and 30-minute quiescent settling to calibrate residual turbidity reduction and establish the optimum economic dosage.

Turbidity = -0.8500 · Dose + 48.00

The governing physical or constitutive relationship was linearized into the coordinate form y = mx + b. Here, the independent coordinate x represents Alum coagulant dosage D (mg/L), and the dependent coordinate y represents Residual settled turbidity (NTU). The gradient m directly determines Turbidity Removal Rate per Unit Coagulant, while the intercept b accounts for baseline tare values or reference offsets. Linear transformation enables robust parameter estimation via ordinary least squares without non-linear numerical divergence. Plotting transformed observation pairs displays structural stiffness, material strength multipliers, soil shear envelopes, or hydraulic ratings directly as linear slopes.

5. Method

  1. Prepare 10 L of synthetic turbid water using bentonite clay; measure initial turbidity (48.0 NTU), pH (7.2), and alkalinity (85 mg/L as CaCO3); pour 1000 mL into each of six jar beakers.
  2. Position beakers under jar test paddles; prepare calibrated alum doses (10, 15, 20, 25, 30, and 35 mg/L) in dosing syringes.
  3. Start paddles at 100 rpm (velocity gradient G ≈ 300 s⁻¹); simultaneously inject alum doses into all six jars; mix for exactly 60 seconds to disperse coagulant.
  4. Reduce paddle speed to 30 rpm (velocity gradient G ≈ 30 s⁻¹); mix gently for exactly 20 minutes to promote inter-particle collisions and floc agglomeration.
  5. Stop paddles and lift drive assembly cleanly; allow water to settle undisturbed for exactly 30 minutes; observe floc settling velocity and supernatant clarity.
  6. Extract 25 mL samples from sampling ports located 2.0 cm below liquid surface; measure residual turbidity in calibrated nephelometer; plot turbidity versus dose.

6. Observations and calculation table

All civil engineering observations use strictly controlled 64-bit IEEE 754 precision buffers. Residuals are computed relative to the ordinary least-squares regression line.

Table 1. Six simulated observations; x and y represent transformed civil engineering metrics.
No.Alum Coagulant Dosage D (mg/L)Residual Settled Turbidity (NTU)Alum coagulant dosage D (mg/L)Residual settled turbidity (NTU)Fitted yResidual
110.039.510.000039.500039.50000.0000
215.035.2515.000035.250035.25000.0000
320.031.020.000031.000031.00000.0000
425.026.7525.000026.750026.75000.0000
530.022.530.000022.500022.50000.0000
635.018.2535.000018.250018.25000.0000

Download the sample observations (CSV) ↓

7. Worked calculation for one observation

For input Alum Dose D = 10.0 mg/L: Measured Residual Settled Turbidity = 39.5000 NTU. Transformed coordinates: independent x = 10.0000, dependent y = 39.5000.

8. Graph, gradient and final calculation

15.067.0021.9714.7528.8822.5035.7830.2542.6938.00Alum coagulant dosage D (mg/L)Residual settled turbidity (NTU)

Circular markers represent empirical structural observations. The solid line represents the ordinary least-squares linear fit.

x̄ = 22.5000; ȳ = 28.8750
Σ(x − x̄)² = 437.5000
Σ(x − x̄)(y − ȳ) = -371.8750
m = Σ(x − x̄)(y − ȳ) / Σ(x − x̄)² = -0.85000000
b = ȳ − mx̄ = 48.00000000
y = -0.8500 · x + 48.0000 ⟹ Target Turbidity Removal Rate per Unit Coagulant = 0.8500 NTU/(mg/L) (theoretical = 0.8500)

9. Uncertainty and comparison

Percentage difference = |estimate − theoretical value| / |theoretical value| × 100 = 0.0000%.

For n = 6 observations, Σresidual² = 0.0000; s² = Σresidual²/(n − 2). Gradient standard error = √[s²/Σ(x − x̄)²] = 0.0000. Intercept standard error = √[s²(1/n + x̄²/Σ(x − x̄)²)] = 0.0000.

Propagating the fit parameters yields a fit standard error of 1.000e-05 NTU/(mg/L), with an ideal coefficient of determination R² = 1.000000.

In civil engineering structural materials testing, geomechanics verification, and hydraulics modeling, empirical uncertainties arise from material microstructural heterogeneity, aggregate packing variations, transducer electronic drift (64-bit IEEE 754 precision digital acquisition), and environmental temperature fluctuations. The ordinary least-squares regression across n = 6 standardized test intervals yields unbiased minimum-variance estimators for both slope and intercept. Because the underlying mechanics—including Hooke's elasticity law, Darcy's porous transport, Bernoulli energy conservation, and Mohr-Coulomb shear strength—adhere strictly to continuum physical principles, residual dispersions remain tightly bounded, yielding an ideal coefficient of determination R² ≥ 0.999999 and confirming the theoretical formulation. Systematic errors (such as machine frame compliance, load cell tare offsets, and temperature drifts) are eliminated using certified calibration standards and differential tare subtraction. Uncertainties in derived moduli, shear strength parameters, and transport coefficients are evaluated via multivariate error propagation.

10. Result and discussion

Turbidity Removal Rate per Unit Coagulant = 0.8500 NTU/(mg/L)
Theoretical reference value: 0.8500 NTU/(mg/L)

The empirical laboratory observations provide rigorous quantitative verification of Coagulation-Flocculation Optimization & Residual Turbidity via Standard Jar Test. In civil engineering mechanics of materials, structural analysis, geotechnical engineering, and hydraulics, physical systems are governed by macroscopic equilibrium, compatibility, and constitutive relationships. Across all six observation trials, the empirical slope m = -0.8500 confirms the theoretical model with near-zero residual variance. Furthermore, comparison with established civil engineering benchmarks (Timoshenko & Gere; Terzaghi & Peck; Chow; Neville; and ASTM standards) underscores vital infrastructure design principles including structural safety factors, serviceability deflection limits, and environmental durability. Residual analysis confirms homoscedastic dispersion without systematic non-linear curvature, validating the underlying model assumptions.

11. Precautions and limitations

The civil engineering physical models apply within the specified calibrated operational window (10.0 to 40.0 mg/L). Tested on synthetic turbid river water (initial turbidity = 48.0 NTU, pH = 7.2, alkalinity = 85 mg/L as CaCO3). Linearized regression over the sub-optimal to optimal dose range correlates residual turbidity to alum dose with slope -0.8500 NTU/(mg/L).

12. Conclusion

This laboratory investigation quantitatively verified the mathematical formulation and physical behavior of Coagulation-Flocculation Optimization & Residual Turbidity via Standard Jar Test. Through rigorous tracking across six observation points, we confirmed an empirical Turbidity Removal Rate per Unit Coagulant of 0.8500 NTU/(mg/L) matching the theoretical reference 0.8500 NTU/(mg/L) within 0.0000% error. The investigation demonstrates why this civil engineering testing method serves as an indispensable cornerstone in infrastructure design, structural safety assurance, and construction quality control.

In-Depth Technical Supplement & Structural Engineering Derivation

1. Objective & Practical Significance

This laboratory investigation optimized the chemical coagulation-flocculation process for surface water purification using a standard six-station jar tester according to ASTM D2035. Across six systematic alum dosages ($D = 10, 15, 20, 25, 30,$ and $35\text{ mg/L}$), settled water residual turbidity was measured to evaluate the removal rate sensitivity slope and identify the optimum economic dosage.

2. Governing Coagulation Models & Linearization

Over the operational dosage range prior to charge restabilization, residual settled turbidity $T$ decreases linearly with alum dose $D$:

\[ T = -k_{turb} \cdot D + T_0 \]

Linear regression yields the turbidity removal sensitivity slope $k_{turb} = 0.8500\text{ NTU/(mg/L)}$ and baseline uncoagulated turbidity $T_0 = 48.00\text{ NTU}$.

3. Experimental Apparatus & Instrumentation Specification

Testing utilized a Phipps & Bird six-station programmable jar tester equipped with stainless steel paddles ($76 \times 25\text{ mm}$) and an illuminated LED base. Supernatant turbidity was analyzed with a Hach 2100Q ratio turbidimeter calibrated against Formazin standards. Sample pH and temperature were logged with an Orion Star A211 pH meter.

4. Standard Operating Procedure & Measurement Protocols

Synthetic river water was prepared with bentonite clay ($T_{initial} = 48.0\text{ NTU}$, $\text{pH} = 7.22$). One-liter aliquots were placed in baffled beakers. Alum was injected simultaneously under rapid mixing ($100\text{ rpm}$, $G = 300\text{ s}^{-1}$) for 60 seconds, followed by slow flocculation ($30\text{ rpm}$, $G = 30\text{ s}^{-1}$) for 20 minutes and quiescent settling for 30 minutes. Supernatant was pipetted from $2.0\text{ cm}$ depth for nephelometric turbidity testing.

5. Safety Analysis, Hazard Mitigation & Personal Protection

Alum is an acidic chemical irritant. Operators wore nitrile gloves, safety glasses, and laboratory coats. Rotating jar tester paddle pinch points were guarded.

6. Raw Experimental Observations & Systematic Data Records

Simulated demonstration data. The following systematic observations were recorded for raw water alkalinity $= 85.0\text{ mg/L as CaCO}_3$:

JarAlum Dose D (mg/L)Raw Turbidity (NTU)Residual Turbidity (NTU)Turbidity Removal (%)Floc Morphology
110.048.039.517.7%Pinpoint micro-flocs, slow settle
215.048.035.226.7%Small dispersed flocs
320.048.031.035.4%Medium flocs, moderate settling
425.048.026.744.4%Well-formed flocs, clear water
530.048.022.553.1%Dense macro-flocs, rapid settling
635.048.018.262.1%Heavy sweep flocs, excellent clarity

7. Quantitative Mathematical Analysis & Regression Models

Linear regression of residual turbidity against coagulant dosage yields:

\[ \text{Turbidity} = -0.85000 \cdot D + 48.00000 \]

with coefficient of determination $R^2 = 1.000000$. The empirical removal rate $k_{turb} = 0.8500\text{ NTU/(mg/L)}$ matches the design standard ($0.00\%$ deviation).

8. Rigorous Error Analysis & Uncertainty Propagation

Turbidimeter instrument uncertainty is $\delta T = \pm 0.1\text{ NTU}$, and pipetted dosage uncertainty is $\delta D = \pm 0.2\text{ mg/L}$. Propagating into removal slope:

\[ \frac{\delta k_{turb}}{k_{turb}} = \sqrt{ \left( \frac{\delta T}{\Delta T} \right)^2 + \left( \frac{\delta D}{\Delta D} \right)^2 } = \pm 0.95\% \]

The calibrated removal sensitivity is $k_{turb} = 0.850 \pm 0.008\text{ NTU/(mg/L)}$.

9. Engineering Discussion & Phenomenological Interpretation

Turbidity decreased monotonically across the tested range as trivalent aluminum cations compressed the diffuse double layer and initiated sweep flocculation. Post-test alkalinity in Jar 6 dropped to $67.5\text{ mg/L}$ ($17.5\text{ mg/L}$ consumed), and pH stabilized at $6.85$, well within the optimal insoluble range for aluminum hydroxide precipitation.

10. Full-Scale Municipal Water Treatment Operation

Water treatment plant operators conduct daily jar tests to adjust chemical coagulant feed pumps in response to storm-induced river turbidity spikes. Selecting the optimal dose minimizes chemical expenditure and prevents sludge dewatering overloads.

11. Self-Assessment Conceptual Questions & Model Answers

Q1: Why is polyaluminum chloride (PAC) increasingly favored over standard alum?
A1: PAC is pre-hydrolyzed, meaning it consumes significantly less natural water alkalinity, functions effectively in cold water, produces lower sludge volumes, and operates across a wider pH range.

Q2: How does temperature affect coagulation kinetics?
A2: Cold water increases water viscosity, retards hydrolysis reaction rates, and slows Brownian particle collision frequencies, requiring higher coagulant dosages or chemical flocculant aids.

12. Concluding Summary & Verified Engineering Metric

The standard Jar Test effectively calibrated coagulation-flocculation performance for turbid surface water. The verified turbidity removal rate $k_{turb} = 0.8500\text{ NTU/(mg/L)}$ ($R^2 = 1.000000$) provides a rigorous empirical basis for municipal chemical dosing control.