키워드, 주문 또는 제품 코드 또는 일련 번호를 검색해 보십시오(예: “CM442” 또는 “기술 정보”).
검색하려면 최소 2자 이상 입력하십시오.

Improve rotary kiln stability through precise combustion control

Process factors, measurement challenges and control requirements for stable rotary kiln operation.

Rotary kiln in cement plant with emission stac
Exterior view of a large rotary kiln at a cement plant entering a building ©Adobe Stock/nordroden
Introduction

Securing rotary kiln stability in high-stakes clinker production

Pyroprocessing is the core of clinker production. A rotary kiln is a large, slightly inclined, slowly rotating cylindrical furnace used to heat and transform raw materials at high temperatures in a continuous process.

The kiln typically accounts for 60-70% of a plant’s total thermal energy use and is the most production‑critical asset in the line. Gas temperatures in the flame zone can reach 1,900 °C, while clinker exits the burning zone at around 1,450 °C. Instruments in this area face dust loads of several hundred grams per cubic meter and chemically aggressive gases containing SO₂, HCl and alkalis. Under these conditions, measurement availability, robustness and maintainability are key requirements.

Stable operation is essential for energy efficiency, consistent clinker quality and predictable maintenance planning. Small variations in combustion, draft or raw mix can shift the process and increase thermal and mechanical stress on the kiln.

This page outlines the factors that influence kiln behavior, the stresses acting on instrumentation and the measurement considerations needed for reliable operation in harsh kiln environments.

핵심 정보

60-70%

of the plant’s total thermal energy is used by a rotary kiln

Rotary kiln process diagram ©Endress+Hauser
Rotary kiln process diagram

Kiln

Process overview

Rotary kiln process in clinker production

The rotary kiln links the preheater and cooler in a continuous thermal process. Raw meal enters the kiln inlet, is heated and sintered in the burning zone and exits as clinker while hot gases flow countercurrent toward the preheater.

Efficient use of thermal energy and prevention of system-wide disturbances require focused preheater and cyclone optimization, reducing blockages and minimizing heat losses. Combustion, draft and material flow remain tightly coupled, so disturbances in one part of the system quickly propagate throughout the entire process line.

Rotary kiln interior with visible burner flame illustrating combustion control and process stability ©Adobe Stock/Drpixel

Measurement challenges in harsh kiln environments

Without reliable process measurements, advanced control strategies lose their ability to anticipate and compensate for process disturbances, forcing the plant to rely more heavily on reactive control actions and conservative operating limits. Maintaining accurate measurements under extreme conditions becomes difficult, especially over prolonged operation.

Instruments must withstand fouling, abrasion, temperature peaks and chemical attack while still delivering stable signals for combustion control and kiln stability.

As measurement quality degrades, signal availability drops, maintenance effort increases and service life shortens. This loss of reliability weakens the control loops that depend on these measurements.

Typical stressors include:

  • High dust load: Gas streams around the kiln and preheater carry dense particulate concentrations that quickly foul optics, plug sampling lines and accelerate drift of exposed sensors. Over time, this reduces signal quality and increases the effort required to keep measurements reliable
  • Particle velocity and abrasive wear: High-speed dust and clinker fines act like a continuous sandblast on probes, optics and housings. Mechanical erosion reduces sensor integrity, weakens protective coatings and increases failure rates in areas such as the kiln hood, riser duct and preheater outlets
  • Extreme temperature exposure: Gas temperatures near the flame can approach 1 900 °C and clinker leaves the burning zone at around 1 450 °C. Even instruments installed at a distance face radiant heat and thermal cycling that can cause drift, premature ageing or complete burnout of sensing elements and electronics
  • Volatile cycles (S, Cl, alkalis): Sulfur, chlorine and alkalis recirculate between the kiln, riser and preheater. These compounds condense and re-evaporate repeatedly, forming sticky deposits that coat sensor surfaces and interfere with signal transmission. They also contribute to corrosion, sensor poisoning and measurement instability, particularly in gas analysis systems
Rotary kiln in cement plant clinker production line with supporting equipment ©Adobe Stock/Mr.B-king
Key measurement points

Critical measurements for kiln efficiency

Stable kiln operation depends on a few core variables that remain measurable despite heat, dust and mechanical stress. The points below outline the critical measurements that provide early visibility into combustion performance, thermal balance and material flow around the kiln:

  • Temperature: Burning zone, hood and secondary air temperatures (indicate flame stability, heat load, clinker sintering behavior)
  • Pressure: Hood pressure and draft/ID fan differential (primary indicators of combustion conditions, air leakage and gas flow consistency)
  • Flow: Secondary/tertiary air and fuel feed flow (controls mixing, burnout efficiency and thermal balance)
  • Level/Build up: Non-contact level or blockage detection at kiln inlet or feed points (radiometric or microwave for harsh areas; prevents feed interruptions and inlet blockages)
  • Gas analysis: Combustion indicators such as O₂/CO/NO/SO₂ (measured at kiln inlet or downstream locations to assess combustion quality and volatile cycle effects)
FAQ

Frequently asked questions on the rotary kiln process stability

The following questions help you learn how process deviations, control strategies and measurement reliability influence rotary kiln stability and clinker production performance. They highlight the key factors that shape combustion behavior, energy efficiency and overall process control in cement plants.

미주