Why Ceramic Slurry Viscosity Suddenly Increases and How to Fix It
By Goway Chemical Technical Team | Updated July 2026 | Ceramic Slip Troubleshooting
Key Takeaways
- Six root causes account for 90%+ of sudden viscosity increases. Water hardness change and clay batch variation are the two most common; temperature drop and bacterial aging are the most frequently overlooked. (Industry-typical reference)
- Adding more deflocculant can make viscosity worse. Over-deflocculation compresses the double layer and causes re-flocculation — the dosage-viscosity curve is U-shaped. Always work from the plateau, not the edge.
- Diagnose before dosing. A 5-minute diagnostic sequence (Ford Cup → pH → hardness → temperature → clay batch) prevents 80% of misdiagnoses and wasted deflocculant.
- FG-MK03 is engineered for viscosity stability. Na₂O 12–15% + SiO₂ 20–22% provides combined electrostatic and steric stabilisation for 24–48 hour storage and hard water conditions. (Source: Goway TDS, FG-MK03)
- Daily Ford Cup logging is the single most effective prevention tool. A 3-second drift over 24 hours is an early warning; a 10-second jump means the process is already out of control.
§1 The 6 Root Causes of Sudden Viscosity Increase
When a slurry that was flowing correctly yesterday suddenly thickens today, the cause is almost always a change in one of six process variables. The diagnostic table below maps each cause to its characteristic symptom, verification method, and immediate corrective action. Use this as your first reference when viscosity drifts.
Diagnostic Table: Cause → Symptom → Verification → Fix
| # | Root Cause | Characteristic Symptom | How to Verify | Immediate Fix |
|---|---|---|---|---|
| 1 | Water hardness change | Viscosity rises across all batches; Ford Cup time increases 5–15 s; deflocculant seems less effective at same dosage | EDTA titration or hardness test kit on current process water; compare to last week's reading. Ca²⁺ + Mg²⁺ > 200 ppm confirms hard water | Add deflocculant at 0.05% steps; if hardness > 200 ppm, consider water softening or switch to FG-MK03 (silicate-buffered) (Source: Goway TDS) |
| 2 | Clay mineral variation | Viscosity rises in specific batches only; correlates with new clay delivery; <2 μm fraction or montmorillonite content changed | Check supplier COA for new clay batch; compare Fe₂O₃, K₂O, L.O.I to previous batch; XRD if available for mineralogy | Adjust deflocculant dosage by ±0.05%; if montmorillonite increased, use FG-SL01A (triple-action); tighten incoming QC |
| 3 | pH drift | Slurry pH outside 7.5–9.0 range; viscosity rises progressively; zeta potential shifts away from optimal negative charge | pH meter on fresh slurry and 24 h stored slurry; compare to target. Drift > 0.5 units is significant | Adjust with dilute NaOH (if acidic) or dilute HCl (if alkaline); check water source pH; see water quality guide |
| 4 | Temperature drop | Viscosity rises in winter or overnight; correlates with ambient temperature; spray dryer inlet also affected | Measure slurry temperature at discharge; compare to previous day. A 10°C drop increases viscosity 15–30% (industry-typical reference) | Insulate storage tanks; maintain mill cooling water temperature; adjust Ford Cup target seasonally; do not over-dose deflocculant |
| 5 | Bacterial activity / aging | Slurry stored > 24 h thickens; sour smell; pH drops; darkened colour; progressive viscosity increase over days | pH test (bacterial activity lowers pH); visual/olfactory check; viscosity at 0 h vs 24 h vs 48 h shows accelerating drift | Discard heavily contaminated slurry; add biocide; shorten storage time; switch to FG-MK03 for long-term stability |
| 6 | Deflocculant degradation / over-dosage | Viscosity rises after adding more deflocculant (over-dose reversal); or STPP stored too long has absorbed moisture and lost activity | Check deflocculant storage conditions (dry, sealed); run lab dosage curve on current deflocculant batch; U-shaped curve confirms over-dosage | Reduce dosage to plateau midpoint; replace degraded STPP; switch to FG-series for better storage stability — see STPP replacement guide |
| Water hardness thresholds and temperature-viscosity relationships are industry-typical reference values. Goway product recommendations are based on Goway Technical Data Sheet specifications. Actual performance is formulation-specific — verify with lab testing. | ||||
§2 Diagnostic Decision Tree: Troubleshooting Flow
When viscosity rises, the order in which you investigate matters. Checking water hardness before clay mineralogy saves time because hardness is faster to test (5 minutes) and more commonly the culprit. Follow this numbered decision flow in sequence.
Step-by-Step Troubleshooting Sequence
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Check Water Hardness (5 min)
Test process water with EDTA titration or a hardness test kit. This is the fastest check and the most common cause.
If hardness > 200 ppm CaCO₃: Water source has changed or seasonal aquifer shift. Add deflocculant at 0.05% steps. For long-term fix, install water softening or switch to FG-MK03 (SiO₂ 20–22%, hard-water tolerant). (Source: Goway TDS)
If hardness < 100 ppm: Proceed to Step 2.
-
Check pH (3 min)
Measure slurry pH with a calibrated pH meter. Target range for most ceramic body slurries: 7.5–9.0.
If pH < 7.0: Acidic shift — likely bacterial activity or acidic water source. Add dilute NaOH to bring pH to 8.0–8.5, then re-check Ford Cup. If pH continues to drop, investigate bacterial contamination.
If pH > 9.5: Alkaline shift — check whether excess deflocculant or alkaline additive was over-dosed. Dilute with fresh water and re-test.
If pH is normal (7.5–9.0): Proceed to Step 3.
-
Check Temperature (2 min)
Measure slurry temperature at the point of use. Compare to the temperature when the slurry was performing normally.
If temperature dropped > 5°C: Seasonal or overnight cooling. A 10°C drop increases viscosity 15–30% (industry-typical reference). Insulate tanks, adjust mill cooling water, or raise storage temperature. Do not add deflocculant to compensate for temperature — it will over-dose when temperature recovers.
If temperature is stable: Proceed to Step 4.
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Check Clay Batch (10–30 min)
Identify whether a new clay delivery coincides with the viscosity increase. Compare supplier COA (Certificate of Analysis) for the current and previous batch.
If new batch differs significantly (Fe₂O₃ ±0.5%, K₂O ±0.3%, L.O.I ±1%, or <2 μm fraction ±3%): Clay mineralogy has shifted. Adjust deflocculant dosage by ±0.05% and run a lab dosage curve. Consider FG-K90 kaolin or FG-B82 ball clay for more consistent raw material performance. (Source: Goway TDS)
If clay batch is unchanged: Proceed to Step 5.
-
Check Deflocculant Dosage (5 min)
Review the dosage log. Has the dosage been increased recently? Was a new deflocculant batch opened?
If dosage was recently increased and viscosity rose: Possible over-deflocculation — the U-shaped curve reversal. Reduce dosage by 0.05% and re-test. See §6 for the dosage-viscosity curve explanation.
If deflocculant batch is new or storage was poor: Possible degradation. STPP absorbs moisture and loses activity over time. Test a fresh sample. Consider switching to FG-series for better storage stability.
If dosage and batch are normal: Proceed to Step 6.
-
Check Storage Time and Bacterial Activity (5 min)
How long has the slurry been stored? Is there a sour smell or colour change?
If stored > 24 h with sour smell or pH drop: Bacterial contamination. Add biocide, shorten storage cycle, or switch to FG-MK03 for 24–48 h stability. (Source: Goway TDS, FG-MK03)
If all six steps are clear but viscosity is still high: Multiple interacting causes may be present. Run a full lab diagnostic: five-point dosage curve with current materials, water analysis, and clay XRD. Contact Goway technical support for assistance.
§3 Water Chemistry Factors: Hardness and pH
Process water is the single most under-monitored variable in ceramic slurry preparation. Yet water chemistry — specifically Ca²⁺/Mg²⁺ hardness and pH — directly determines how effectively your deflocculant works. A change in water source, seasonal aquifer shift, or even a new recycled-water ratio can destabilise a slurry that was running perfectly the day before.
How Hardness Ions Neutralise Deflocculant
Calcium (Ca²⁺) and magnesium (Mg²⁺) ions are multivalent cations that interfere with deflocculation through two mechanisms:
- Direct complexation: Ca²⁺ and Mg²⁺ form insoluble complexes with phosphate-based deflocculants (like STPP), consuming the active ingredient before it can act on clay particles. Each Ca²⁺ ion can sequester one STPP molecule, effectively removing it from the system.
- Double-layer compression: Multivalent cations compress the electrical double layer around clay particles much more aggressively than monovalent Na⁺. This reduces zeta potential magnitude and eliminates the repulsive force that keeps particles dispersed — causing flocculation.
Water Hardness Classification and Response
| Hardness Level | CaCO₃ (ppm) | Effect on Slurry | Recommended Deflocculant Strategy |
|---|---|---|---|
| Soft | < 100 | Standard deflocculant performance; low ionic interference | All FG-series grades work at standard 0.2–0.5% dosage (Source: Goway TDS) |
| Medium | 100–200 | Mild ionic interference; may require 10–20% higher dosage; 24 h stability slightly reduced | FG-MK03 or FG-SL01A — silicate buffer improves tolerance |
| Hard | > 200 | Severe interference; STPP rapidly consumed; viscosity instability; 24 h drift exceeds 20% | FG-MK03 (SiO₂ 20–22%) + consider water softening; monitor hardness daily |
| Very hard | > 400 | Most deflocculants ineffective; slurry cannot reach target viscosity at reasonable dosage | Water softening mandatory; blend softened water with raw water to target < 150 ppm |
| Hardness thresholds are industry-typical reference values. Actual impact depends on clay mineralogy, body formulation, and deflocculant chemistry. FG-MK03 hard-water tolerance is based on Goway TDS product positioning. | |||
How pH Drift Affects Zeta Potential
The zeta potential of clay particles is pH-dependent. Below the isoelectric point (IEP), clay surfaces carry a positive charge; above it, they carry a negative charge. For most ceramic clays, the IEP falls between pH 2–4, so at normal processing pH (7.5–9.0), clay surfaces are negatively charged and deflocculant works by enhancing this negative charge.
When pH drifts below 7.0, the negative charge weakens, zeta potential approaches zero, and particles begin to flocculate. When pH rises above 9.5, excess OH⁻ ions can interfere with certain deflocculant mechanisms. The optimal pH window for most body slurries is 8.0–8.8 (industry-typical reference).
For a comprehensive explanation of the electrostatic mechanisms behind deflocculation, see our beginner's guide to zeta potential in ceramic slurries. For detailed water quality monitoring protocols, see our guide to the impact of water quality on ceramic slip.
§4 Clay and Raw Material Variability
Clay is a natural mineral, and batch-to-batch variation is inevitable. The three parameters that most affect slurry viscosity are: (1) the ratio of kaolinite to illite to montmorillonite, (2) the <2 μm fine fraction percentage, and (3) the soluble salt content (K₂O, Na₂O, CaO). A shift in any of these can change slurry viscosity even when the deflocculant dosage remains constant.
Three Key Clay Variability Factors
| Factor | What Changes | Viscosity Impact | Mitigation |
|---|---|---|---|
| Mineralogy ratio | Kaolinite / illite / montmorillonite proportions shift between batches | Montmorillonite (smectite) has 10–20× the surface area of kaolinite and absorbs far more water — even a 2% increase in montmorillonite can raise viscosity significantly | XRD mineralogy on each new clay delivery; maintain buffer stock; adjust deflocculant ±0.05% |
| <2 μm fraction | Fine particle percentage varies; affects surface area and colloidal behaviour | Higher <2 μm fraction = more surface area to disperse = higher deflocculant demand. A 3% increase in fines may require 0.05–0.10% more deflocculant (industry-typical reference) | Particle size analysis on incoming clay; sedimentation test; adjust dosage based on fines content |
| Soluble salts | K₂O, Na₂O, CaO content varies; affects ionic strength and double layer | High soluble CaO acts like water hardness from within the clay — compresses double layer and consumes deflocculant. K₂O affects viscosity and firing behaviour | Check COA for K₂O, Na₂O, CaO; wash clay or blend batches to average out variation |
Goway Clay Products for Consistent Performance
FG-K90 Kaolin Whiteness 90.0
High-whiteness kaolin with controlled particle size distribution. Whiteness 90.0 ensures consistent fired body colour, reducing the need for whiteness compensation when switching deflocculants.
- Best for: Wall tile, porcelain tile, sanitaryware where whiteness is critical
- QC advantage: Tighter mineralogy control than generic kaolin sources
Source: Goway TDS, FG-K90. Product page: /products_detail/5.html
FG-B82 Ball Clay High Plasticity
High-plasticity ball clay with consistent mineralogy. Provides the binding and plasticity needed for green body strength, with controlled fine-fraction content for predictable viscosity behaviour.
- Best for: Body formulations requiring high green strength and consistent slurry rheology
- QC advantage: Batch-to-batch <2 μm fraction controlled to tighter tolerance
Source: Goway TDS, FG-B82. Product page: /products_detail/5.html
When clay variability is the root cause of viscosity fluctuations, the most effective long-term strategy is to establish a raw material QC protocol that catches variation before it enters production. For a comprehensive approach to additive-related problems, see our guide to troubleshooting common ceramic additive problems.
§5 Temperature and Seasonal Effects
Temperature is the most frequently overlooked cause of viscosity increase because it changes slowly and invisibly. Unlike a water hardness spike or a bad clay batch, a seasonal temperature drop does not trigger an alarm — it just gradually thickens the slurry until someone notices the Ford Cup time has crept up by 5–8 seconds.
The Temperature-Viscosity Relationship
Ceramic slurry viscosity follows an Arrhenius-type relationship with temperature: as temperature decreases, the kinetic energy of water molecules decreases, inter-particle attraction becomes relatively stronger, and viscosity increases. The practical rule of thumb for ceramic body slurry:
Winter vs. Summer Slurry Behaviour
| Parameter | Summer (30–38°C) | Winter (10–18°C) | Corrective Action | |
|---|---|---|---|---|
| Ford Cup flow time | Lower — slurry appears thinner | Higher — slurry appears thicker | Set seasonal target ranges: summer 22–26 s, winter 26–32 s (adjust to your body) | |
| Deflocculant demand | Lower — heat aids dispersion | Higher — cold inhibits ion exchange | Do NOT increase dosage by more than 0.05% for winter; risk of over-dose when temperature rises | |
| 24 h viscosity drift | Higher — bacterial activity accelerates in heat | Lower — bacterial activity slows in cold | Summer: shorten storage, add biocide. Winter: focus on temperature stability | |
| Spray dryer interaction | Inlet air hotter; slurry atomises easier | Inlet air colder; atomisation less efficient; powder moisture may rise | Adjust spray dryer inlet temperature seasonally; monitor powder bulk density | |
| Ball mill discharge temperature | May exceed 40°C — reduce mill cooling | May fall below 20°C — increase cooling water temperature or insulate mill | Target 25–35°C at discharge for consistent deflocculant performance | |
| Temperature-viscosity relationships and seasonal behaviour patterns are industry-typical reference values. Actual sensitivity depends on solid content, clay type, and deflocculant chemistry. | ||||
For spray dryer optimisation across seasonal conditions, see our guide on maximizing spray dryer output.
§6 Deflocculant Dosage Issues: Over, Under, and Degradation
Deflocculant dosage is a double-edged sword. Too little, and the slurry is under-deflocculated and viscous. Too much, and the slurry is over-deflocculated — which paradoxically also becomes viscous through double-layer compression and re-flocculation. Understanding the U-shaped dosage-viscosity curve is essential for diagnosing whether your problem is too much or too little.
The Dosage-Viscosity Curve (U-Shaped)
Three Dosage Problems and Their Symptoms
| Problem | Symptom | How to Diagnose | Fix |
|---|---|---|---|
| Under-deflocculation | High viscosity; slurry thick; poor flow; Ford Cup time above target | Add 0.05% deflocculant — if viscosity drops, you were under-dosed. Run lab dosage curve to find plateau | Increase dosage in 0.05% steps until plateau is reached; target plateau midpoint |
| Over-deflocculation | Viscosity increased after adding deflocculant; slurry may appear stringy or gel-like; Ford Cup time rose despite more chemical | Reduce dosage by 0.05% — if viscosity drops, you were over-dosed. U-shaped curve confirms it | Reduce dosage to plateau midpoint; never add more deflocculant to a slurry that thickened after dosing |
| Deflocculant degradation | Same dosage produces higher viscosity than before; progressive loss of effectiveness; STPP clumped or discoloured | Check storage: STPP absorbs moisture, hydrolyses, loses activity. Test fresh vs. stored deflocculant in lab | Replace degraded deflocculant; improve storage (dry, sealed, <30°C); consider switching to FG-series |
STPP vs. FG-Series: Storage Stability Comparison
| Property | STPP | FG-Series (FG-2017 / MK03 / N203B / SL01A) |
|---|---|---|
| Moisture sensitivity | High — STPP is hygroscopic; absorbs moisture and hydrolyses to pyrophosphate and orthophosphate, losing deflocculation activity | Moderate — silicate-based composition is less hygroscopic; FG-MK03 and FG-SL01A with SiO₂ 18–22% show better storage stability (Source: Goway TDS) |
| Shelf life (sealed, dry) | 6–12 months before measurable activity loss (industry-typical reference) | 12+ months under proper storage (Source: Goway product page) |
| Shelf life (opened bag, humid) | 2–3 months — clumping and hydrolysis begin | 4–6 months — less prone to clumping |
| Cost vs. STPP | 100% (baseline) | 30–40% of STPP cost (Source: Goway product page, /products_detail/6.html) |
| STPP replacement | — | 100% replacement at 0.2–0.5% dosage (Source: Goway TDS) |
| Storage stability comparisons are industry-typical reference values. FG-series product data is from Goway TDS. Actual shelf life depends on storage temperature, humidity, and packaging integrity. | ||
For the complete STPP-to-FG-series transition protocol, including lab dosage curve methodology and pilot trial framework, see our STPP replacement factory trial guide.
§7 Immediate Fix Protocol: 5-Step Emergency Response
When the slurry is thickening and production is at risk, you need a fast, safe response. This 5-step protocol is designed to restore flow within 30–60 minutes without risking over-deflocculation. The key principle: measure first, dose incrementally, stop when target is reached.
-
Step 1: Measure Ford Cup Flow Time (2 min)
Use Ford Cup #4 at the current slurry temperature (record the temperature). Measure three times and take the average. Compare to your target range.
Decision rule: If Ford Cup is within ±3 s of target → no action needed; monitor. If > 3 s above target → proceed to Step 2. If > 10 s above target → this is a severe increase; proceed to Step 2 but also prepare for clay batch investigation (Step 5).
-
Step 2: Check pH (3 min)
Measure slurry pH with a calibrated pH meter. Normal range: 7.5–9.0.
If pH < 7.0: Add dilute NaOH (10% solution) gradually while stirring, re-checking pH every 30 seconds. Target pH 8.0–8.5. Then re-measure Ford Cup — the pH correction alone may restore flow.
If pH > 9.5: Possible over-deflocculation. Skip to Step 4 but add deflocculant in smaller 0.02% increments. Better yet, dilute with a small amount of fresh water first.
If pH is normal: Proceed to Step 3.
-
Step 3: Check Water Hardness (5 min)
Test current process water with EDTA titration or a hardness test kit. Compare to your last recorded value.
If hardness increased > 50 ppm from baseline: Water source has changed. Add deflocculant at 0.05% steps (Step 4). For long-term fix, investigate water source and consider switching to FG-MK03 (SiO₂ 20–22%, hard-water tolerant). (Source: Goway TDS)
If hardness is normal: Proceed to Step 4.
-
Step 4: Add Deflocculant Incrementally (10–20 min)
Add deflocculant at 0.05% steps on dry body weight. After each addition, stir for 5 minutes, wait 5 minutes for equilibration, then measure Ford Cup.
Stop when: Ford Cup returns to target ±2 s.
Maximum total addition: 0.15% above current dosage. If viscosity has not returned to target after 0.15% total addition, stop adding deflocculant — further dosing risks over-deflocculation. Proceed to Step 5.
Product choice for emergency fix: FG-2017 (Na₂O 30–32%) provides the fastest viscosity reduction for immediate response. (Source: Goway TDS, FG-2017)
-
Step 5: Investigate Clay Batch and Storage (if Step 4 fails)
If 0.15% additional deflocculant did not restore flow, the problem is not dosage — it is material or environment.
Check: (a) Was a new clay delivery used? Compare COA to previous batch. (b) How long has the slurry been stored? If > 24 h, check for bacterial activity (smell, pH drop, colour). (c) Has the slurry temperature dropped > 5°C?
If clay batch is the cause: Adjust body formulation — blend new clay with buffer stock of old batch. Run a lab dosage curve with the new clay to establish the correct dosage.
If bacterial contamination: Add biocide; discard slurry if severely contaminated. Switch to FG-MK03 for better long-term stability in future batches.
If temperature drop: Do NOT add more deflocculant. Warm the slurry or adjust the Ford Cup target for the current temperature.
§8 Long-Term Prevention Strategy
Emergency fixes keep production running today, but recurring viscosity problems indicate a systemic gap in process control. The following four-pillar prevention strategy eliminates the root causes of sudden viscosity increase and reduces the frequency of emergency interventions.
Pillar 1: Install Hardness Monitoring
Water hardness is the #1 cause of sudden viscosity increase, yet most factories test it only when problems occur. Install a simple online hardness monitor or implement a daily hand-test protocol. The investment is minimal; the payoff is early detection of water source changes before they affect production.
| Monitoring Method | Frequency | Cost Level | Detection Capability |
|---|---|---|---|
| Hand test kit (EDTA drops) | Daily, each shift | Low | Detects changes > 20 ppm |
| Benchtop hardness titration | Weekly + when problems occur | Low–Medium | Detects changes > 5 ppm; identifies Ca²⁺ and Mg²⁺ separately |
| Online hardness monitor | Continuous | Medium–High | Real-time detection; can trigger alarms |
Pillar 2: Use FG-MK03 for 24–48 Hour Stability
For slurries that are stored more than 12 hours before use — whether for shift changes, weekend storage, or batch scheduling — the deflocculant must maintain viscosity stability over time. FG-MK03 is engineered specifically for this purpose.
FG-MK03 Long-Term Stability
Na₂O 12–15% + SiO₂ 20–22%. The silicate component adsorbs on clay particle edges, forming a protective layer that maintains inter-particle repulsion for 24–48 hours. This is the recommended grade for any slurry that sits in storage.
- Dosage: 0.2–0.5% on dry body weight (Source: Goway TDS)
- Best for: Stored slurry, hard water, shift-change storage, weekend hold
- STPP replacement: 100% at 30–40% of STPP cost
Source: Goway TDS, FG-MK03. Product page: /products_detail/6.html
FG-2017 Fast Emergency Response
Na₂O 30–32%, highest in the series. Pure electrostatic deflocculation via rapid Na⁺ ion exchange. Best for immediate viscosity reduction when speed matters more than long-term stability.
- Dosage: 0.2–0.5% on dry body weight (Source: Goway TDS)
- Best for: Fast dispersion, emergency viscosity reduction, high-throughput lines
- Caution: No SiO₂ buffer — less tolerant of hard water; blend with FG-MK03 for stability
Source: Goway TDS, FG-2017. Product page: /products_detail/6.html
Pillar 3: Implement Daily Ford Cup Logging
A daily Ford Cup log is the simplest, cheapest, and most effective early-warning system for viscosity problems. Record flow time, slurry temperature, and pH at the same time each day. A 3-second drift over 24 hours is an early warning; a 10-second jump means the process is already out of control.
Pillar 4: Establish Raw Material QC Protocol
Tighten incoming QC on kaolin and ball clay to catch mineralogy variation before it enters production. The following monitoring parameters should be checked on every new clay delivery:
| Parameter | Why It Matters for Viscosity | Test Method | Acceptance Tolerance |
|---|---|---|---|
| Fe₂O₃ content | Affects fired colour; high Fe₂O₃ may correlate with impurity clays that affect rheology | XRF or wet chemistry | ±0.3% from baseline |
| K₂O content | Soluble K⁺ acts as a flocculant; high K₂O increases deflocculant demand | XRF or AAS | ±0.2% from baseline |
| L.O.I (Loss on Ignition) | Indicates organic matter content; high L.O.I may signal bacterial contamination risk | Thermogravimetric (1100°C) | ±1.0% from baseline |
| <2 μm fraction | Directly affects surface area and deflocculant demand | Sedimentation or laser diffraction | ±3% from baseline |
| Mineralogy (XRD) | Montmorillonite content is the single biggest viscosity driver | X-ray diffraction | Montmorillonite ±2% from baseline |
| pH of clay slurry (10% in water) | Acidic clays consume deflocculant; alkaline clays may interfere with pH control | pH meter on 10% suspension | 5.5–8.0 (typical for kaolin/ball clay) |
| Tolerances are industry-typical reference values. Establish your own baseline from 3–5 consecutive acceptable batches, then set tolerances based on the observed variation. For consistent raw material performance, consider Goway FG-K90 kaolin and FG-B82 ball clay — see /products_detail/5.html. | |||
Complete Monitoring Parameter Table
| Parameter | Monitoring Frequency | Target Range | Corrective Action |
|---|---|---|---|
| Ford Cup flow time | Every batch (or every 4 h) | ±3 s of target | > 3 s: investigate; > 5 s: emergency protocol (§7) |
| Slurry pH | Every 8 h | 7.5–9.0 | Adjust with dilute acid/base; check water source if persistent |
| Slurry temperature | Every 4 h | 25–35°C | Insulate tanks; adjust mill cooling; set seasonal targets |
| Water hardness | Daily (or weekly if stable) | < 150 ppm CaCO₃ | > 200 ppm: switch to FG-MK03; consider water softening |
| 24 h viscosity drift | Daily | ≤ 15% increase | > 15%: switch to FG-MK03; check for bacterial activity |
| Deflocculant dosage | Every batch | 0.2–0.5% (plateau midpoint) | If creeping upward: investigate root cause, do not keep increasing |
| Solid content | Every 8 h | ±0.5% of target | Adjust water addition; verify deflocculant dosage is not compensating for solids change |
| Clay batch COA | Every new delivery | Within tolerance (see above) | Out of tolerance: blend with buffer stock or reject delivery |
| These monitoring parameters form the core of a viscosity prevention programme. Implement them progressively — start with Ford Cup, pH, and water hardness, then add the others as routine becomes established. | |||
For complementary strategies on improving pressing performance and green body quality alongside viscosity control, see our guides on improving dry press strength and fast cast vs. traditional casting.
§9 Frequently Asked Questions
The most common cause of overnight viscosity increase is bacterial activity and slurry aging — microorganisms degrade organic components and alter pH, destabilising the deflocculant. Other frequent causes include water hardness changes (if the factory switched water sources), temperature drop overnight (a 10°C drop can increase viscosity 15–30%), and deflocculant degradation in storage. To diagnose: measure Ford Cup flow time, check pH against the previous day, test water hardness, and measure slurry temperature. If pH has drifted more than 0.5 units or hardness has increased, address the root cause before adding more deflocculant.
Calcium (Ca²⁺) and magnesium (Mg²⁺) ions in hard water neutralise deflocculant by forming insoluble complexes with phosphate-based dispersants and by compressing the electrical double layer around clay particles. Soft water (<100 ppm CaCO₃) allows deflocculants to work at standard dosage. Medium-hard water (100–200 ppm) may require 10–20% higher dosage. Hard water (>200 ppm) can cause severe viscosity increase and may require water softening or a silicate-buffered deflocculant such as FG-MK03 (SiO₂ 20–22%). For detailed water quality guidance, see our article on the impact of water quality on ceramic slip.
Yes. Over-deflocculation compresses the electrical double layer around clay particles too aggressively, eliminating the repulsive forces that keep particles dispersed. This causes re-flocculation and a viscosity increase — the classic U-shaped dosage-viscosity curve. The solution is to reduce dosage, not add more. Always work from a lab dosage curve (five-point test) to identify the minimum-viscosity plateau, and operate at the middle of the plateau for maximum tolerance to variation. Goway FG-series deflocculants (FG-2017, FG-MK03, FG-N203B, FG-SL01A) all show this U-shaped behaviour at 0.2–0.5% dosage.
FG-MK03 (Long-Term Stability Deflocculant) is engineered specifically for 24–48 hour slurry stability. Its Na₂O 12–15% / SiO₂ 20–22% composition provides combined electrostatic deflocculation and silicate-layer steric stabilisation, which maintains inter-particle repulsion over extended storage. FG-SL01A (Na₂O 18–20% / SiO₂ 18–20%) is a versatile alternative for factories with variable body formulations. Both are 100% STPP replacements at 0.2–0.5% dosage. For fast immediate viscosity reduction rather than long-term stability, FG-2017 (Na₂O 30–32%) is the preferred choice.
A 10°C temperature drop typically increases ceramic slurry viscosity by 15–30% (industry-typical reference). This means a slurry that flows at 25 seconds Ford Cup #4 at 30°C may rise to 29–33 seconds at 20°C. Seasonal transitions are the most common cause of temperature-related viscosity increase. The fix is not to add more deflocculant — instead, insulate slurry storage tanks, maintain ball mill cooling water temperature, and adjust the Ford Cup target range seasonally. In winter, consider switching to FG-MK03 for better low-temperature stability.
Follow a 5-step emergency protocol: (1) Measure Ford Cup flow time to quantify the increase. (2) Check slurry pH — if drifted more than 0.5 units, adjust with dilute acid or base. (3) Check water hardness — if above 200 ppm CaCO₃, investigate water source change. (4) Add deflocculant incrementally at 0.05% steps (on dry body weight), measuring Ford Cup after each addition — stop when viscosity returns to target. (5) If no response after 0.15% total addition, investigate clay batch variation or bacterial contamination. Never add a large deflocculant dose at once — this can cause over-deflocculation and further viscosity increase.
Get a Customised Viscosity Troubleshooting Plan
Send us your current slurry parameters and our technical team will diagnose the likely cause of your viscosity increase and recommend the optimal FG-series deflocculant grade and dosage. No generic advice — a plan built for your specific process conditions.
View FG-Series Ceramic Deflocculant Products →To submit an inquiry, visit our Ceramic Deflocculant product page and use the inquiry form. Please reference this guide when submitting. Samples with TDS, SDS, and COA are available.
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