I. Process Background
Limestone slurry is the “ammunition” that the WFGD system uses to consume SO2. Powdered limestone (CaCO3) is conveyed by belt or pneumatic means into a powder silo, then fed by a dosing valve at a set rate into the slurry preparation tank, where it is mixed with process water under agitation to produce a limestone slurry with a mass concentration of approximately 20%–30%. This slurry is subsequently pumped through long pipelines to the absorption tower to participate in the desulfurization reaction.
The slurry concentration directly determines the calcium-to-sulfur ratio (Ca/S) within the absorption tower—too high a concentration results in an excess of CaCO3 being fed per unit time, with unreacted particles leading to waste and exacerbating scaling inside the tower; too low a concentration, on the other hand, compromises desulfurization efficiency, causes SO2 emissions to exceed limits, and sharply increases environmental compliance risks. Therefore, online density measurement of the slurry at the outlet of the preparation tank or on the feed line to the absorption tower is a “critical” parameter for optimizing energy consumption and ensuring environmental compliance in the flue-gas desulfurization system.
II. Pain Points of Traditional Density Measurement Solutions
• Limestone slurry is highly abrasive (the fine limestone particles are very hard). Conventional insertion-type tuning fork, Coriolis, rotor, or diaphragm differential pressure instruments exhibit significant wear after just 6 to 12 months of operation, resulting in zero‑point drift and reduced measurement range.
• The slurry preparation system experiences frequent start‑stops, and prolonged residence times in the pipelines promote settling and scaling. Contact-style instruments are particularly sensitive to fouling, requiring shutdowns for cleaning one to two times per month.
• Although mass flow meter‑based density meters offer reliable accuracy, their use in limestone slurry applications—where processes are well‑established and safety and compliance requirements are increasingly stringent—is gradually being phased out.
• Lagging or unstable measurement data prevent the PLC/DCS from implementing precise “water addition/powder addition” closed‑loop control, leaving operations dependent on manual adjustments by巡检工s and resulting in large fluctuations in slurry concentration.
III. PS7000 Solution
The PS7000 is installed via flange at the outlet of the slurry preparation tank (or on the main discharge line of the transfer pump), using ultrasonic acoustic impedance technology to measure slurry density in a non‑contact manner. It transmits real‑time data to the PLC/DCS system, enabling automatic closed‑loop regulation of powder feed rates and make‑up water volumes to maintain slurry concentration within the process‑set target range.

Figure 2: Schematic diagram of online density measurement and closed‑loop control in the limestone slurry preparation section
Key Technical Advantages of the PS7000 in This Process Condition ▸ Customized wear-resistant probe: 316L / 2205 duplex stainless steel combined with special ceramics, surface roughness Ra ≤ 0.4μm, smooth and anti-scaling; ▸ Non-contact ultrasonic measurement principle, unaffected by limestone powder abrasion, probe service life ≥ 5 years; ▸ 0–80% mass concentration, full-scale linear measurement, accuracy ±1% FS, resolution 0.001 g/cm³, meeting fine-control requirements; ▸ Supports 4G remote transmission (optional), enabling the central control room and operations & maintenance center to view historical curves and operating status in real time; ▸ Built-in 20,000-cycle data storage and 400 log entries; no data loss upon power failure, ensuring traceability for fault analysis. |
IV. Customer Value
Comparison Dimensions | Original differential pressure / tuning fork solution | PS7000 Solution |
Concentration Control Accuracy | ± 3%–5% variation | ± 1%FS stable output |
Instrument service life | 6–12 months of wear | ≥ 5 years of maintenance-free operation |
Shutdown Cleaning Frequency | 1–2 times per month | No shutdown required |
Closed-loop control response | Data drift · Difficult to achieve closed-loop control | Second-level response · Automatic closed loop |
Overall SO2 removal rate | High fluctuation | Stable ≥ 95% |
Limestone powder consumption rate | Slightly high | Decreased by approximately 3%–8% |
In a limestone slurry preparation system serving a 2×600 MW generating unit, after three months of PS7000 commissioning, slurry concentration variability decreased from ±5% to within ±1%. Operators reported, “Powder addition is now largely determined automatically by the system, eliminating reliance on empirical adjustments.” The unit achieved substantial annual savings in limestone powder and water consumption while significantly reducing the risk of scaling in the desulfurization tower.