Skip to main content

Boiler Systems: Troubles in Operation and Their Causes

Definition of boiler systems

Boiler system is a system that is used to heat water and to generate required steam or hot water.

The boiler system is generally composed of the following units:

(a) Feedwater treatment unit: demineralizer, etc.

In case that the raw water is supplied from a river, a lake and so on, the raw water treatment units (clarifier, filter,etc.) are required. 

(b) Feedwater line,

(c) Deaerator,

(d) Boiler including preheater, superheater and desuperheater,

(e) Steam and condensate line,

(f) Condensate treatment unit,

(g) Wastewater treatment unit,

(g) Chemical injection unit.

Classification of boilers by their structures

(1) Cylindrical boilers (pressure : below 20 kgf/cm2) :

(a) Vertical boilers,

(b) Flue-tube boilers,

(c) Fire-tube boilers,

(d) Fire and flue-tube boilers.

(2) Water-tube boilers :

(a) Natural circulation boilers (pressure : low to high),

(b) Forced circulation boilers (pressure : low to high),

(c) Once-through boilers (pressure : above 75 kgf/cm2),

(d) Mini-circulation boilers (packaged type) (pressure : below 30 kgf/cm2).

A typical structure of a water-tube boiler

 

A typical water flow of boiler system


Troubles in Boiler System Operation and Their Causes

Kinds of
problems

Troubles in boiler system
operation

Causes of troubles

Scaling

Reduction of boiler efficiency, Expansion or bursting of heating tubes by overheating.

Leakage of hardness, silica, etc., from softeners or demineralizers, Inadequate blowdown control, Inadequate chemical treatment.

Corrosion

Corrosion damages of boiler systems including feedwater, steam and condensate lines, Scaling troubles caused by corrosion products.

Insufficient deaeration of feedwater,
Inadequate oxygen scavenger treatment,
Insufficient pH control of feedwater, boiler water and condensate.

Carryover

Reduction of steam quality,
Reduction of turbine efficiency by scaling,
Reduction of product quality treated by the steam.

Excess concentration of boiler water,
Contamination of boiler water with organic substances,
Fluctuation of boiler operation load,
Defects of steam separator.

Carryover: Transferring of dissolved solids in boiler water into the steam line.

Comments

Popular posts from this blog

Understanding the Causes of Pump Shaft Breakage

By NTS. Pump shafts are essential in many industrial and commercial applications, providing the necessary mechanical force to move fluids through pipelines and process systems. However, when a pump shaft breaks, it can cause significant downtime, production losses, and safety risks. In this article, we will explore the common causes of pump shaft breakage and how to prevent it from occurring. 1. Excessive Load  The most common cause of pump shaft breakage is excessive load. When a pump is overloaded, it places a significant amount of stress on the shaft, causing it to bend, warp, or break. Overloading can be caused by a variety of factors such as a clogged discharge line, worn impeller, or damaged bearings. Proper maintenance, regular inspections, and monitoring of the pump's performance can help prevent overloading. 2. Misalignment  If the pump and motor are not properly aligned, it can cause stress on the pump shaft and lead to breakage. Misalignment can occur due ...

Why Pump Shafts Often Break at the Keyway Area

By NTS Pump shaft failure can lead to significant downtime and repair costs in industrial plants. One of the most common locations for pump shaft failure is at the keyway area. In this article, we will explore the reasons why pump shafts often break at the keyway and what can be done to prevent such failures. The keyway is a high-stress point (weakest point)  on the shaft, where a key is inserted to transmit torque between the shaft and the pump impeller or coupling. During operation, the keyway experiences cyclic loading that creates a bending moment in the shaft, which is concentrated in the keyway area. Over time, this cyclic loading can cause fatigue failure in the shaft material, leading to a fracture at the keyway. In addition to cyclic loading, other factors can contribute to shaft failure at the keyway. Improper keyway design or installation can lead to stress concentrations or inadequate clearance between the key and keyway . Misalignment or overloading can also cause ex...

The 7 guiding principles of a Maintenance 4.0 strategy

Formulating a digital strategy is not easy, but these guidelines can help you get off the sidelines and into the game. By Eitan Vesely and Deddy Lavid (Ben lulu), Presenso It is not uncommon for organizations to struggle with many issues related to digitalization. With the hype around digitalization at fever pitch, it is easy to become overwhelmed by the multitude of options available in the marketplace. But the strongest contributing factor to implementation challenges is a failure to devise a strategy for an extensive period of uncertainty. Formulating a Maintenance 4.0 strategy is not easy. An aggressive strategy based on overinvesting in unproven technologies or a conservative strategy of merely waiting on the sidelines are unrealistic options. Guiding principles The seven guiding principles for a Maintenance 4.0 strategic plan are: 1. Invest based on the business case The primary obligation to shareholders does not change just because of the changes occurring within t...

Dry Gas Seal Failure Modes

BY BHUSHAN NIKAM. Invented in the mid-20th century and typically equipped in process gas centrifugal, dry gas screw compressors and expanders, dry gas seals (DGS) are the preferred gas lubricated dry seal solutions available on the market. They have become the standard for new machines. DGS are robust, simple, consume less power, and are more efficient in reducing leakage than their predecessor. Various configurations such as tandem with and without an intermediate labyrinth ( Figure 1 ), single ( Figure 2 ), and double ( Figure 3 ) are available & shall be selected based on process requirements. In this article, we discuss the various DGS failure modes and how they should be addressed:  PRESSURIZED HOLD/STANDBY Pressurized hold, also called settle-out condition, occurs when the compressor remains at a standstill, but the casing is pressurized. If an alternate process gas lacks sufficient pressure and flow, process gas enters the seal cavity through the process labyrinth ...

Dry-Running Sealing Technology: Pump Applications (P2)

Solutions to Common Problems The operation of a single contacting seal would be difficult with any of the identified problems. A single contacting seal relies on cooling and lubrication from the process liquid being sealed. Any interruption in the cooling and lubrication processes will result in damage to the seal and leakage to the environment. The non-contacting, dry-running seal is a solution to many of the problems identified by users. An installation to a pump is illustrated in Figure 2. This type of pump seal technology does not require the circulation of liquid for cooling. Instead, a static heat of an inert gas is used to pressurize the space between the seals. Nitrogen gas in normally used to create the barrier between the process liquid and the environment. The gas barrier pressure is normally 20 to 30 psi/1.4 to 2 bar above the seal chamber pressure.  The spiral groove geometry of the seal face is responsible for lift-off and separation of the seal f...