Fremont Industries, Inc.
  Technical Support Series

(800) 436-1238 
sales@fremontind.com 

 
Understanding Boiler System Waterside Deposits
(PDF Version)

  

Boilers, cooling towers and heat exchangers are notoriously susceptible to deposit formation due to the presence of  a variety    of impurities in the process water.  Deposit formation in this equipment may result in:

  • A decrease in heat transfer.
  • Loss in system’s energy efficiency.
  • Unplanned down-time/loss of production.
  • Increased fuel or energy costs.
  • Increased maintenance expenses.
  • Component failure and/or premature replacement.
  • Dangerous system operating conditions.
  • Increased insurance costs. 

An understanding of deposits and the prevention of their formation may result in:

  • Cleaner heat transfer surfaces.
  • Increased system efficiency.
  • Maximized economy of operation.
  • System maintenance cost savings.
  • Greater system life.
  • Safer working conditions.

 

CLASSIFICATION OF DEPOSITS

Deposits found in steam generation and related equipment fall into three primary groups; true scale deposits, scale like deposits, and sludge or sedimentary deposits.

True Scale

By definition, a true scale deposit  is a macrocrystalline growth held together by intercrystalline bonding forces.   True scale may be either crystalline or amorphous (possessing no definite crystalline structure).  True scales are the result of dissolved substances from a supersaturated solution.  The formation of true scale deposits is relative to physical and chemical system variables.

Scale-Like Deposits

Scale-like deposits may be crystalline or amorphous, in structure.

These scale-like deposits form by the deposition of precipitated suspended solids from the bulk water solution.  Typically, scale-like deposits are bonded by ionic or static charges existing between the individual particles of the deposit.  Most frequently, the formation of scale-like deposits is relative  to the agglomeration of suspended solids at a point of evaporation, low flow velocity area or dehydration.

Sedimentary or Sludge Deposits

Sedimentary or sludge deposits are formed by the agglomeration of suspended matter present in the bulk water.  Sludges differ from true scale and scale-like deposits in that their formation is primarily affected by the physical (as opposed to the chemical) characteristics of the system.  Sludges are typically comprised of contaminants present in the make-up water, process contaminants, and by-products of corrosion processes.  These deposits influence the formation of true scale and scale-like deposits. 

Examples  
Boiler Scale Boiler Sludge Oxygen Attack on
Boiler Metal
 

 

DEPOSIT CONSTITUENTS, CAUSES AND PREVENTION - BOILER SYSTEMS

Compound

Possible Causes

Preventive Measures

Calcium Carbonate

  • Insufficient phosphate residual.
  • Insufficient sludge.
  • Excessive suspended solids and/or dissolved solids.
  • Maintain proper alkalinity, phosphate and sludge residuals in boiler.
  • Maintain proper solids levels through cycles of concentration control by blowdown.
  • Pretreatment of make‐up water.

Calcium Hydroxyapatite

  • Excessive suspended and/or dissolved solids.
  • Insufficient sludge conditioners residuals.
  • Maintain proper solids levels through cycles of concentration control blowdown.
  • Maintain proper sludge conditioner residuals.
  • Pretreatment of make‐up water.

Calcium Phosphate

  • Excessive phosphate residual.
  • Low alkalinity residuals.
  • Excessive suspended and/or dissolved solids.
  • Maintain proper phosphate, “P”, “M” and “OH” alkalinity residuals in boiler.
  • Maintain proper solids levels through cycles of concentration control by blowdown.

Calcium Sulfate

  • Insufficient phosphate or polymer level.
  • Poor blowdown control.
  • Maintain proper sulfate level through proper blowdown.
  • Increase sludge conditioner dosage.

Carbamates

  • Amine carbamate formation (typically cyclohexylamine).
  • Use diethylaminoethanol as return line treatment.

Copper Oxides

  • Galvanic corrosion of cuprous metal.
  • Excessive return line treatment feed (amine corrosion of cuprous metal).
  • Boiler water carryover into steam/condensate system.
  • Use of dielectric unions in multimetal systems.
  • Maintain proper return line pH and return line treatment residuals.
  • Eliminate boiler water carryover through blowdown and/or antifoam.

Iron Oxides

  • Make‐up water infiltration.
  • Corrosion of ferrous.
  • System metal:
  • ‐condensate system
    ‐boiler system
    ‐preboiler system

  • Galvanic corrosion.
  • Pretreatment of make‐up water.
  • Maintain proper condensate pH.
  • Maintain proper residuals of oxygen scavenger and alkalinity in boiler water.
  • Treat pre-boiler sections with oxygen scavenger.
  • Use of dielectric unions in nonmetal systems.

Iron Phosphate

  • Excessive phosphate residual.
  • Excessive iron contamination (see iron oxides).
  • Reduce iron contamination (as above).
  • Reduce phosphate residual.
  • Employ non‐phosphate conditioner residuals.

Magnesium Carbonate

  • Low hydroxide residual.
  • Maintain proper hydroxide alkalinity residual.

Magnesium Phosphate

  • Excessive phosphate residuals.
  • Insufficient hydroxide alkalinity residual.
  • Maintain proper phosphate and hydroxide alkalinity residuals in boiler water.
  • Pretreatment of make‐up water.

Organic Matter

  • Contamination by oil, process contaminants, “cow water”.
  • Eliminate process contamination.
  • Add organo sludge conditioners.
  • Add antifoam.
  • Monitor “cow water” organic levels.

Serpentine

  • Excessive suspended and/ or dissolved solids.
  • Insufficient sludge conditioners residuals.
  • Maintain proper solids levels through cycles of concentration control by blowdown.
  • Maintain proper sludge conditioner residuals.

Silica

  • Excess silica concentration.
  • Maintain proper solids through cycles of concentration control by blowdown.
  • Pretreatment of make‐up water.

 

DEPOSIT SAMPLING TECHNIQUES

The first step in gathering useful information from a deposit analysis is the careful collection of a truly representative sample of the deposit.  Deposit samples should be forwarded to the laboratory with attention paid to the following: 

  • Every effort should be made to remove the deposit in its natural state.  Do not crush, dry, treat or otherwise alter the deposit sample prior to forwarding to the laboratory.
     
  • Caution must be taken so as not to remove under-deposit materials such as base metals, plastics, or wood.
     
  • If deposit analysis trend data is to be valid, deposit sample must be removed from the same locations over a predetermined period of time.
     
  • As much accompanying data as can be gathered should be forwarded with the deposit sample (location, products in use, system condition, etc.).  Excessive data is never a hindrance; insufficient data can be.
     
  • The deposit samples should be sent to the laboratory for analysis as soon as possible following the removal.   Timeliness is extremely crucial in cases where biological fouling is suspected.

 

SCALE REMOVAL OPTIONS

Alkalinity Treatments
Alkaline treatments are typically used to remove gases, oils, and organic contaminants.  Alkaline treatments are of particular value in the preoperational cleaning of new systems.

Acidic Descalers (Off Line) 
Acidic treatments are effective in the removal of carbonate scales and corrosion by-product deposits.  The acids most commonly used include hydrochloric (muriatic), sulfuric, citric and sulfamic; often containing a corrosion inhibitor.

In-Service Deposit Removal Treatments
In-service treatments offer a non-acid option for the removal of inorganic salts.  Deposit cleaning during system operation is particularly advantageous in situations involving systems which cannot be shut down for acid or alkaline cleaning procedures.

  

Effects of Scale

 

Scale
Thickness
Inches

Fuel Loss, % of Total Use

Scale Type

Normal

High Iron

Iron Plus Silica

1/64

1.0

1.6

3.5

1/32

2.0

3.1

7.0

3/64

3.0

4.7

11.0

1/16

3.9

6.2

13.0