Bioceramics, energy technologies and sustainable design
**Guiding question:** How can ceramic selection account for interfaces, service life and life-cycle evidence?
§8.1 Why this unit matters to ceramic engineering
Guiding question: How can ceramic selection account for interfaces, service life and life-cycle evidence?
A proposed energy device replaces a metallic component with a ceramic one whose production needs more thermal energy but might last longer. This is a question about service interfaces and environmental accounting and the distinction between material performance versus lifecycle claims. A defensible answer identifies feedstock composition, chemistry, processing path and microstructure before comparing measured properties. It also names the potentially controlling failure mode: a recipe that optimizes density, dielectric response or simple bend strength can still worsen thermal cycling, porosity topology, lifetime or chemical compatibility. The technical sections below connect simplified mathematics to the kinds of measurements that would justify a practical claim.
Chemical compatibility, performance life, emissions and manufacturability demand different evidence streams. Biomedical claims must be validated with biological safety requirements; environmental claims demand full comparative boundaries.
Track product mass, reject rate, processing energy and service durability separately. A synthetic release curve and emissions-per-kilogram proxy do not demonstrate clinical performance or sustainability.
§8.2 Measurement and conservation checkpoints
Write down the starting composition, defect-sensitive atmosphere and powder or glass history; define whether reported fractions are by area, mass, moles or volume; and record the process history that could alter process traceability and functional unit. For any local observation, describe why its sampling plan represents the part. Treat unmeasured durability or yield losses as an explicit rival explanation and plan held-out service tests and audited inventory as an independent check.
§8.3 Bioceramic bioactivity and hydroxyapatite interfaces
Scientific foundation
Calcium phosphates, alumina and zirconia appear in different biomedical contexts because composition alone does not define their biological role. Hydroxyapatite can be osteoconductive under appropriate surface and biological conditions, but bone bonding, dissolution, mechanical load and sterilization history require separate evaluation. The Ca/P atomic ratio is a useful stoichiometric descriptor yet cannot demonstrate bioactivity or phase purity. Surface topography and protein adsorption can mediate outcomes in ways not predicted by bulk modulus.
Governing relationship or decision rule: For a narrowly illustrative one-compartment process, released fraction f=1-exp(-kt), not a physiological dissolution law. Read every term in the equation as part of a declared specimen condition. In bioceramic bioactivity and hydroxyapatite interfaces, a valid calculation requires the state of the ceramic, unit system and physical or geometrical meaning of each quantity. A nominally identical oxide composition can conceal different dopant distributions, porosity, grain-boundary glass and processing damage. Equal bulk density does not guarantee equivalent fracture, transport or thermal stability. Interpret measurements only after identifying which feature of the state they can support.
Worked ceramic investigation
Prepare a synthetic hydroxyapatite dissolution curve using a declared first-order proxy, then compare what an actual phosphate and calcium release assay would need to measure. Ask how scaffold porosity might aid biological access while undermining load-bearing strength. Design relevant biocompatibility testing rather than describing a simulated release fraction as an in vivo response.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 9.428571 day, the declared formula returns 28.107627 % released; at Elapsed time = 17.85714 day, it returns 46.473857 % released. On this interval the modeled value increases, and the two-point slope is 2.1790443 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
The browser expression is 100(1-Math.exp(-0.035t)). Model validity is limited to: One-compartment constant-rate coefficient 0.035 per day; educational curve only, not a physiological bioactivity or clinical kinetics claim. Reproduce the first result with a calculator using the expression and units stated here. Before accepting the number, check the units analytically and identify what is being held constant. If a result looks realistic, that coincidence does not establish physical validation. Try an extreme permitted slider input and ask whether the computed change is physically interpretable or an artifact of the simplifying assumptions.
Evidence, uncertainty, and a competing mechanism
Laboratory dissolution in one buffered solution does not predict tissue response, long-term fatigue or patient outcomes. Clinical claims require appropriately validated medical-device evidence.
Exercises and self-assessment
Exercise 8.1A — Physical mechanism. Why does a chemical match to bone mineral not automatically imply a safe load-bearing implant? State one plausible explanation, one competing explanation and the material-state observation that separates them. Relate the claim to the governing relationship written above rather than merely repeating definitions.
Exercise 8.1B — Numerical cross-check. Recalculate 28.107627 % released from the companion formula at 9.428571 day and compare with 46.473857 % released at 17.85714 day. State the sign of the sensitivity and explain whether the changed input would reasonably be controlled independently in a real ceramic specimen.
Exercise 8.1C — Test design. Propose a preparation or test matrix that addresses unmeasured durability or yield losses. Give the specimen orientation, spatial sampling scheme, temperature-time record and principal instrument calibration. Explain which observation would falsify your first hypothesis and name a condition under which your model should not be used.
§8.4 Dental and orthopedic zirconia degradation
Scientific foundation
Partially stabilized zirconia is used where favorable strength, toughness and aesthetics are sought, but its mechanical properties depend on composition, processing and phase stability. Moisture at elevated temperature can promote low-temperature degradation in susceptible formulations through tetragonal-to-monoclinic transformation, sometimes causing roughening and microcracking. Polishing, grinding, surface treatments and aging history can affect strength independently of the bulk crystal phase.
Governing relationship or decision rule: Local phase fraction and flaw population jointly affect reliability; neither a hardness number nor the presence of tetragonal grains alone is a safety certificate. Read every term in the equation as part of a declared specimen condition. In dental and orthopedic zirconia degradation, a valid calculation requires the state of the ceramic, unit system and physical or geometrical meaning of each quantity. A nominally identical oxide composition can conceal different dopant distributions, porosity, grain-boundary glass and processing damage. Equal bulk density does not guarantee equivalent fracture, transport or thermal stability. Interpret measurements only after identifying which feature of the state they can support.
Worked ceramic investigation
Compare surface-polished and roughened zirconia coupons after a defined accelerated aging schedule. Measure phase fractions and surface roughness before and after, then conduct fracture and wear testing while keeping geometry and loading history comparable. Record why autoclave exposure is only an accelerated laboratory indicator, not a direct calendar-to-clinical lifetime conversion.
A companion calculator called Electricity-only manufacturing CO2 proxy supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Furnace electricity per product mass = 3 kWh/kg, the declared formula returns 1.35 kg CO2e/kg; at Furnace electricity per product mass = 4.4 kWh/kg, it returns 1.98 kg CO2e/kg. On this interval the modeled value increases, and the two-point slope is 0.45 kg CO2e/kg per kWh/kg. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
The browser expression is 0.45*E. Model validity is limited to: Assumed grid factor=0.45 kg CO2e/kWh; excludes embodied raw materials, upstream energy, rejected yield, transport, life cycle and date-specific grid data. Reproduce the first result with a calculator using the expression and units stated here. Before accepting the number, check the units analytically and identify what is being held constant. If a result looks realistic, that coincidence does not establish physical validation. Try an extreme permitted slider input and ask whether the computed change is physically interpretable or an artifact of the simplifying assumptions.
Evidence, uncertainty, and a competing mechanism
Dental and orthopedic applications have different constraints and regulatory evidence. Any specific claim about implants, sterility or patient outcomes needs product-level validation and clinical review.
Exercises and self-assessment
Exercise 8.2A — Physical mechanism. What simultaneous measurements are needed to separate hydrothermal transformation damage from grinding cracks? State one plausible explanation, one competing explanation and the material-state observation that separates them. Relate the claim to the governing relationship written above rather than merely repeating definitions.
Exercise 8.2B — Numerical cross-check. Recalculate 1.35 kg CO2e/kg from the companion formula at 3 kWh/kg and compare with 1.98 kg CO2e/kg at 4.4 kWh/kg. State the sign of the sensitivity and explain whether the changed input would reasonably be controlled independently in a real ceramic specimen.
Exercise 8.2C — Test design. Propose a preparation or test matrix that addresses unmeasured durability or yield losses. Give the specimen orientation, spatial sampling scheme, temperature-time record and principal instrument calibration. Explain which observation would falsify your first hypothesis and name a condition under which your model should not be used.
§8.5 Cementitious ceramics and hydration products
Scientific foundation
Hydraulic cement evolves from reactive clinker and supplementary materials into a porous binder assemblage containing calcium-silicate-hydrate and other hydrates. Water-to-binder ratio, curing temperature, moisture history and pore connectivity all affect strength and ingress, while aggregate properties and dimensional changes govern concrete behavior. Carbonation or chloride exposure cannot be described as simply a good or bad reaction without examining reinforcement, alkalinity and transport context.
Governing relationship or decision rule: In a mix balance, water/binder mass ratio is m_water/m_cementitious; transport depends on connectivity and curing, not merely total water. Read every term in the equation as part of a declared specimen condition. In cementitious ceramics and hydration products, a valid calculation requires the state of the ceramic, unit system and physical or geometrical meaning of each quantity. A nominally identical oxide composition can conceal different dopant distributions, porosity, grain-boundary glass and processing damage. Equal bulk density does not guarantee equivalent fracture, transport or thermal stability. Interpret measurements only after identifying which feature of the state they can support.
Worked ceramic investigation
Establish a notional concrete mix with identical binder composition but different curing moisture histories. Compare compressive strength, sorptivity and chloride migration indicators rather than treating a single strength result as a durability guarantee. Quantify powder input and emissions using a transparent bill of materials, not one generic low-carbon label.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 26.28571 day, the declared formula returns 60.148096 % released; at Elapsed time = 34.71429 day, it returns 70.328999 % released. On this interval the modeled value increases, and the two-point slope is 1.2079037 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
Evidence, uncertainty, and a competing mechanism
Cement chemistry is outside the direct applicability of high-temperature sintering models. The release-rate slider illustrates only a mathematical curve and does not reproduce cement hydration kinetics.
Exercises and self-assessment
Exercise 8.3A — Physical mechanism. Why might a high early compressive strength coexist with poor long-term chloride resistance? State one plausible explanation, one competing explanation and the material-state observation that separates them. Relate the claim to the governing relationship written above rather than merely repeating definitions.
Exercise 8.3B — Numerical cross-check. Recalculate 60.148096 % released from the companion formula at 26.28571 day and compare with 70.328999 % released at 34.71429 day. State the sign of the sensitivity and explain whether the changed input would reasonably be controlled independently in a real ceramic specimen.
Exercise 8.3C — Test design. Propose a preparation or test matrix that addresses unmeasured durability or yield losses. Give the specimen orientation, spatial sampling scheme, temperature-time record and principal instrument calibration. Explain which observation would falsify your first hypothesis and name a condition under which your model should not be used.
§8.6 Solid oxide cells, porous electrodes and interfaces
Scientific foundation
Solid oxide fuel and electrolysis cells require dense electronically blocking electrolytes and porous electrodes with connected pathways for charge, gas and reaction sites. Electrode performance depends on microstructure, chemistry and interfacial polarization, not just bulk ionic conductivity. Thermal expansion mismatch and redox cycles can damage seals, electrodes or interfaces. Because operating modes differ, lifetime claims for fuel-cell operation cannot be copied without testing electrolysis duty cycles.
Governing relationship or decision rule: Cell voltage loss can be decomposed approximately into reversible potential, ohmic drop and electrode overpotentials under stated current and composition. Read every term in the equation as part of a declared specimen condition. In solid oxide cells, porous electrodes and interfaces, a valid calculation requires the state of the ceramic, unit system and physical or geometrical meaning of each quantity. A nominally identical oxide composition can conceal different dopant distributions, porosity, grain-boundary glass and processing damage. Equal bulk density does not guarantee equivalent fracture, transport or thermal stability. Interpret measurements only after identifying which feature of the state they can support.
Worked ceramic investigation
Define a cell-stack diagnostic with impedance spectra at several gas partial pressures and thermal histories. Compare electrolyte thickness while holding electrode architecture fixed, then test for electronic leakage and gas crossover separately. Develop a degradation ledger that distinguishes ohmic, electrode and contact contributions instead of attributing all voltage loss to oxygen vacancies.
A companion calculator called Electricity-only manufacturing CO2 proxy supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Furnace electricity per product mass = 5.8 kWh/kg, the declared formula returns 2.61 kg CO2e/kg; at Furnace electricity per product mass = 7.2 kWh/kg, it returns 3.24 kg CO2e/kg. On this interval the modeled value increases, and the two-point slope is 0.45 kg CO2e/kg per kWh/kg. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
Evidence, uncertainty, and a competing mechanism
Simplified Arrhenius temperature models do not predict chemical degradation, contact resistance, electrode exchange currents or stack lifetime. Hazard controls and specialist equipment are essential for actual hot-cell testing.
Exercises and self-assessment
Exercise 8.4A — Physical mechanism. What observation would distinguish electrolyte cracking from electrode passivation when voltage falls? State one plausible explanation, one competing explanation and the material-state observation that separates them. Relate the claim to the governing relationship written above rather than merely repeating definitions.
Exercise 8.4B — Numerical cross-check. Recalculate 2.61 kg CO2e/kg from the companion formula at 5.8 kWh/kg and compare with 3.24 kg CO2e/kg at 7.2 kWh/kg. State the sign of the sensitivity and explain whether the changed input would reasonably be controlled independently in a real ceramic specimen.
Exercise 8.4C — Test design. Propose a preparation or test matrix that addresses unmeasured durability or yield losses. Give the specimen orientation, spatial sampling scheme, temperature-time record and principal instrument calibration. Explain which observation would falsify your first hypothesis and name a condition under which your model should not be used.
§8.7 Life-cycle assessment and circular ceramic manufacturing
Scientific foundation
Energy-intensive calcination and high-temperature firing can dominate some ceramic processes, but raw-material extraction, water use, rejects, transport and end-of-life handling also matter. An environmental comparison must declare functional unit, boundary and performance requirements. A longer-lived ceramic part can outperform a lower-emissions part per kilogram when replacements and failure consequences are included; the reverse may hold if waste and firing energy are high. Recycling routes depend on contamination and phase chemistry.
Governing relationship or decision rule: Illustrative scope-2 proxy m_CO2e=(kWh per kg)*(kg CO2e per kWh); full LCA uses declared boundaries, allocation and function. Read every term in the equation as part of a declared specimen condition. In life-cycle assessment and circular ceramic manufacturing, a valid calculation requires the state of the ceramic, unit system and physical or geometrical meaning of each quantity. A nominally identical oxide composition can conceal different dopant distributions, porosity, grain-boundary glass and processing damage. Equal bulk density does not guarantee equivalent fracture, transport or thermal stability. Interpret measurements only after identifying which feature of the state they can support.
Worked ceramic investigation
Use the simple manufacturing-electricity carbon proxy with a variable energy demand per kilogram and fixed illustrative grid intensity. Then build a full accounting worksheet adding raw materials, reject rate, recycled feedstock processing and lifetime replacement scenarios. Calculate emissions per verified service hour or component function as well as per kilogram.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 43.14286 day, the declared formula returns 77.909002 % released; at Elapsed time = 51.57143 day, it returns 83.552554 % released. On this interval the modeled value increases, and the two-point slope is 0.66957398 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
Evidence, uncertainty, and a competing mechanism
The proxy is not a life-cycle assessment and its grid factor is hypothetical, not a present-day regional measurement. Comparison requires data quality, allocation rules and sensitivity analysis.
Exercises and self-assessment
Exercise 8.5A — Physical mechanism. Under what conditions can reducing furnace temperature increase rather than lower total life-cycle impacts? State one plausible explanation, one competing explanation and the material-state observation that separates them. Relate the claim to the governing relationship written above rather than merely repeating definitions.
Exercise 8.5B — Numerical cross-check. Recalculate 77.909002 % released from the companion formula at 43.14286 day and compare with 83.552554 % released at 51.57143 day. State the sign of the sensitivity and explain whether the changed input would reasonably be controlled independently in a real ceramic specimen.
Exercise 8.5C — Test design. Propose a preparation or test matrix that addresses unmeasured durability or yield losses. Give the specimen orientation, spatial sampling scheme, temperature-time record and principal instrument calibration. Explain which observation would falsify your first hypothesis and name a condition under which your model should not be used.
§8.8 Integrated investigation: Select a ceramic with defensible service impacts
The evidence problem
A proposed energy device replaces a metallic component with a ceramic one whose production needs more thermal energy but might last longer. The problem cannot be solved by selecting the equation that gives the most convenient number. First define which property must be achieved, the physical constraint that could prevent it, and the microstructural condition of the specimen being evaluated. List known facts separately from inferred mechanisms, uncertain constants and quantities not yet measured. The central decision is not simply which powder process or ceramic composition seems attractive: it is what observations would allow a researcher or an engineer to prefer one explanation over competing causes.
Integrated analysis and model workflow
Compare equal service function, reliability, manufacturing yield, repairability, emissions and actual operating conditions. Build a minimal processing–structure–property map linking the material history with observed state and relevant response. Carry the distinction between service interfaces and environmental accounting and material performance versus lifecycle claims through the map. For phase equilibria, show composition conservation and do not infer processing kinetics from a phase diagram. For a densification relation, separate pore disappearance from neck growth and grain coarsening. For electrical function, distinguish ion migration, electronic leakage, electrode polarization and nonlinear ferroelectric switching. Use the actual specimen time–temperature history instead of only a furnace setting. For damage, compare local flaw driving force with the appropriate fracture resistance.
Validation plan, report, and counterfactual
Construct uncertainty bounds for embodied impacts and a transparent durability-test program on comparable components. Include an alternative interpretation capable of explaining the same first observation and choose a different instrument or held-out processing condition that separates it. State which measurement would cause you to reject the favored hypothesis. Retain raw counts, image scales, processing logs and sample identifiers. If comparing ceramic families, write down the constraints that matter for weight, stiffness, temperature, oxidation and availability rather than reporting only one maximum strength metric.
Known limits: A carbon proxy cannot establish a product sustainability claim. A reader should be able to reconstruct the entire inference from original specimen provenance and measured inputs. The synthetic datasets intentionally contain no physical replicate scatter or hidden model mismatch; those omissions would make a real-world confidence interval far wider than a formula plot suggests.
Five cumulative exam questions
- Draw a cause-and-effect diagram linking composition, process history, service interfaces and environmental accounting and the decision-controlling property; mark one arrow that cannot yet be established from the observations.
- Write a conservation or constitutive relation for material performance versus lifecycle claims with all units and physical validity assumptions; interpret one limiting case.
- Propose two mutually exclusive experimental signatures for the favored and competing mechanisms and name the required independent instruments.
- Show how unmeasured durability or yield losses could reverse a seemingly beneficial result, and design the minimum additional test needed to detect that reversal.
- Write a one-paragraph evidence statement specifying what has been demonstrated, what is merely predicted, and which industrial decision is unjustified until qualification.
Step-by-Step Statistical Simulation and Monte Carlo Solutions
Three original questions connect calculations, definitions and interpretation. Open each solution to follow the reasoning.
Prepare a synthetic hydroxyapatite dissolution curve using a declared first-order proxy, then compare what an actual phosphate and calcium release assay would need to measure. Ask how scaffold porosity might aid biological access while undermining load-bearing strength. Design relevant biocompatibility testing rather than describing a simulated release fraction as an in vivo response.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 9.428571 day, the declared formula returns 28.107627 % released; at Elapsed time = 17.85714 day, it returns 46.473857 % released. On this interval the modeled value increases, and the two-point slope is 2.1790443 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
The browser expression is 100(1-Math.exp(-0.035t)). Model validity is limited to: One-compartment constant-rate coefficient 0.035 per day; educational curve only, not a physiological bioactivity or clinical kinetics claim. Reproduce the first result with a calculator using the expression and units stated here. Before accepting the number, check the units analytically and identify what is being held constant. If a result looks realistic, that coincidence does not establish physical validation. Try an extreme permitted slider input and ask whether the computed change is physically interpretable or an artifact of the simplifying assumptions.
Compare surface-polished and roughened zirconia coupons after a defined accelerated aging schedule. Measure phase fractions and surface roughness before and after, then conduct fracture and wear testing while keeping geometry and loading history comparable. Record why autoclave exposure is only an accelerated laboratory indicator, not a direct calendar-to-clinical lifetime conversion.
A companion calculator called Electricity-only manufacturing CO2 proxy supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Furnace electricity per product mass = 3 kWh/kg, the declared formula returns 1.35 kg CO2e/kg; at Furnace electricity per product mass = 4.4 kWh/kg, it returns 1.98 kg CO2e/kg. On this interval the modeled value increases, and the two-point slope is 0.45 kg CO2e/kg per kWh/kg. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
The browser expression is 0.45*E. Model validity is limited to: Assumed grid factor=0.45 kg CO2e/kWh; excludes embodied raw materials, upstream energy, rejected yield, transport, life cycle and date-specific grid data. Reproduce the first result with a calculator using the expression and units stated here. Before accepting the number, check the units analytically and identify what is being held constant. If a result looks realistic, that coincidence does not establish physical validation. Try an extreme permitted slider input and ask whether the computed change is physically interpretable or an artifact of the simplifying assumptions.
Establish a notional concrete mix with identical binder composition but different curing moisture histories. Compare compressive strength, sorptivity and chloride migration indicators rather than treating a single strength result as a durability guarantee. Quantify powder input and emissions using a transparent bill of materials, not one generic low-carbon label.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 26.28571 day, the declared formula returns 60.148096 % released; at Elapsed time = 34.71429 day, it returns 70.328999 % released. On this interval the modeled value increases, and the two-point slope is 1.2079037 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
Define a cell-stack diagnostic with impedance spectra at several gas partial pressures and thermal histories. Compare electrolyte thickness while holding electrode architecture fixed, then test for electronic leakage and gas crossover separately. Develop a degradation ledger that distinguishes ohmic, electrode and contact contributions instead of attributing all voltage loss to oxygen vacancies.
A companion calculator called Electricity-only manufacturing CO2 proxy supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Furnace electricity per product mass = 5.8 kWh/kg, the declared formula returns 2.61 kg CO2e/kg; at Furnace electricity per product mass = 7.2 kWh/kg, it returns 3.24 kg CO2e/kg. On this interval the modeled value increases, and the two-point slope is 0.45 kg CO2e/kg per kWh/kg. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.
Use the simple manufacturing-electricity carbon proxy with a variable energy demand per kilogram and fixed illustrative grid intensity. Then build a full accounting worksheet adding raw materials, reject rate, recycled feedstock processing and lifetime replacement scenarios. Calculate emissions per verified service hour or component function as well as per kilogram.
A companion calculator called Synthetic fractional release supplies a separate, deliberately limited numerical experiment. Its controls isolate one effect so a reader can check dimensions and sensitivity instead of guessing the direction of change. At Elapsed time = 43.14286 day, the declared formula returns 77.909002 % released; at Elapsed time = 51.57143 day, it returns 83.552554 % released. On this interval the modeled value increases, and the two-point slope is 0.66957398 % released per day. These are worked calculations, not fabricated experimental observations or certified properties of any real ceramic formulation.