Boiler water treatment -EHSQ--ADVANTAGES OF HELAMIN

	Use of a combination of environment-compatible agents in a patented formulation
	Affects the structure of the protective magnetite layer in the boiler so to increase protection
	The system is protected against corrosion as a membrane is formed
	Gentle removal of existing scaling from calcium carbonate and corrosion products
	Economical and ecological alternative to conventional water conditioning
	The salt content of boiler water is not increased
	Reduction of water blow down rate
	Disperses dirt, mineral salts and iron oxide
	Alkalinizes the entire steam system including condensate recirculation and feed water systems
	Simple analysis for determining the Helamin,content of the boiler water and condensate
	Energy-saving thanks to improved heat transfer

Boiler water treatment chemicals  Water is the essential medium for steam generation. Conditioning it properly can increase the efficiency of boiler and as well as extend the boiler’s life. Treating boiler water also insures safe and reliable operation: without proper treatment, severe problems can develop, some so severe that boiler itself can be destroyed. Boiler water problem generally falls into classes: deposit related and corrosion related. Because the two often interact, it is very common to find a boiler experiencing both simultaneously. There are many instances where deposit causes corrosion and corrosion causes deposits. The other problem is of steam purity.  Therefore the aim of the boiler water treatment chemical is  1)      To prevent the formation of scales  and deposits on heating surface  2)      To prevent corrosion in the boiler and steam system.  3)      To maintain high level of steam purity.  The pressure and design of boiler determines the quality of water it requires for steam generation. The sequence of treatment depends on the type and concentration of the contaminants found in water supply and the desired quality of finished water to avoid three major problems in boiler systems – Deposits, Corrosion and Carryover.   Scaling One of the aims of boiler water treatment is to prevent the formation of scales and deposits in the boiler systems. Scale can be prevented by external method or by conditioning with internal treatment. At times combination of both external and internal treatment is done. Water gets evaporated due to high heat transfer rate. This concentrates the water and scale precipitates. The type of scale will depend upon the chemical composition of the concentrated water. Scales formed in boiler systems can be divided into four groups:- 1.   Scale due to calcium  & magnesium 2.   Scale due to iron oxide  3.   Scale due to copper  4.   Scale due to silica The combination in which they exist will not be same. It will vary from boiler to boiler. In some boiler the scale can be due to Calcium and in some due to Iron.  Scale forms as the solubilities of the scale forming salts in water decreases and the temperature and concentration increases. When feed water temperature is elevated to boiler water temperature, the solubility of scale forming salt is decreased, and solid scale begins to form on the boiler system. Thus we can say that Scale formation is a function of two criteria:- (a) The concentration and solubility limits of the dissolved salts. (b) The retrograde solubility (inversely proportional to temperature) characteristics of some salt.   Causes of deposit formation in boiler water Boiler deposits result from the impurities carried in with feed water. Their source is either make up water containing mineral salt, condensate containing process contaminants, corrosion products or in the case of condensers – in leaking cooling water. Deposits can also be formed due to the internal chemicals used.   Corrosion   Corrosion is the destructive attack of metal by chemical or electrochemical reaction. Corrosion is always because of chemical reaction. Physical deterioration is termed as erosion, wear or galling. Deterioration can be due to both chemical and physical attack.  Water corrosiveness is determined by the impurities present in it. Oxygen, dissolved solids, and dissolved acids in water attack the common construction material. Alkali can also be corrosive, at high temperature, as in boiler. Problems due to corrosion 1.   Thining of metal   2.   Development of crack 3.   Pitting of metal 4.   Metal perforation 5.   interference with heat transfer 6.   Contamination of water Corrosion is a complex problem and many factors influence corrosion. The factors to be considered are physical, chemical and biological. Factors influencing corrosion Physical Factors 1.      System construction   3.      Temperature 5.      Water Chemistry 2.      System Pressure   4.      Flow Velocity   Chemistry plays a very important role in corrosion. We have already explained earlier that corrosion is electrochemical reaction and is influenced by chemical factors like pH, alkalinity, dissolved salts and others.   a) Alkalinity Alkalinity in water is due to presence of Bicarbonates, carbonates and hydroxyl ions.  In raw water alkalinity is mainly due to bicarbonates.  Some times carbonates ions may also be present.  Carbonates and particularly hydroxyl ions are rarely encountered in untreated waters.  Hydroxyl ions normally get introduced during treatment of water. Alkalinity is determined by using standard acid solution using methyl or phenolphthalein indicator.  Alkalinity determined by using methyl orange indicator is termed as M-Alkalinity or Total Alkalinity.  P-Alkalinity is determined by using phenolphthalein as indicator.  The different type of alkalinity present in water supplies can be calculated from M and P-Alkalinity value determined by titration. Alkalinity is the ability of natural water to neutralize acid.  This happens because of buffering mechanism. Alkalinity in raw water is primarily composed of bicarbonates and carbonates. Acid compounds having free h+ ions react with CO3 and HCO3 ions and conversely Oh ions also reacts with CO3 and HCO3 ions.                            CO32-  + H+  ®  HCO3-                            HCO3-   + H+ ®H2CO3                              HCO3-  + OH- ® CO32- + H2O In either case acid or base is neutralized by the carbonate or bicarbonate. Thus it can be seen that when  Acid (or caustic ) is added to water having high concentration of bicarbonate or carbonate the pH of water  does not change much compared to when the same amount of acid(or caustic) is added to pure water. This is known as buffering capacity.   b) pH   When pure water dissociates, the number of hydrogen ions is equal to number of hydroxyl ions. Such a solution is called neutral solution. pH is defined as negative logarithm of H+ ions. Solution having pH less than 7 are acidic and those greater than 7 are basic. Low pH is Corrosive and   high pH is protective to pipe. Very high can cause scaling and deposits. c)      Dissolved Oxygen   Oxygen is considered has one of the most corrosive components in water chemistry. Dissolved O2 with traces of chlorides or solids can cause pitting corrosion of metallic surface.  The resulting condition may be severe, even at low pressure. d)      Dissolved Solids   Dissolved solids or salt content of water present as ion increases electrical conductivity  of water. Higher the conductivity, greater the potential for corrosion. Some salts like CaCO3 are involved in scale forming and thereby reducing corrosion. e)      Hardness Hardness is generally associated with scale forming. Hardness is composed primarily of Ca &  Mg  ions but may also include other metallic ions like iron and manganese. All hardness ions have the property of forming scales. One of the methods for corrosion control is by planned deposition of CaCO3 f)    Chloride & Sulphate   Chloride and sulphate ions inhibit the formation of scale by keeping hardness ions in solution. Trace amount of Chlorides even with dissolved oxygen can cause corrosion in boiler.   Type Of Corrosion   The type of corrosion classified with respect to outward appearance or altered physical properties are Uniform attack Pitting  Cavitations erosion  Dezincification & parting  Intergrannular corrosion  Cracking   Oxygen Corrosion Water coming out of deaerators has residual oxygen. As explained earlier even a trace amount of oxygen can cause corrosion. This last trace of oxygen is removed chemically. Sodium Sulphite and hydrazine or one of its product is used for removal of residual oxygen. Sodium Sulphite is used for low pressure boiler. Amine is preferred  in high pressure boiler because it does not add to TDS, unlike Sodium Sulphite. Effect of pH Both high and low pH can cause corrosion in boiler. In acidic range the protective layer of magnetite is not able to form and it cause corrosion. In very high pH range the protective layer of magnetite breaks down and this leads to caustic corrosion. For corrosion prevention maintaining proper pH and alkalinity is very important. Acid Corrosion Excess acid cause damage at more rapid rate than excess base. Simply because this happens, it should not be taken as an operating guideline. Magnetite film forms due to corrosion but once formed adhere tightly and acts as a barrier between boiler water and steel. Acids are capable of destroying this film and hence water chemistry must be so maintained that the protective film is not disrupted. This can be done by keeping the water in alkaline range. Caustic Corrosion. Feed water is maintained at alkaline pH. Alkali is added to provide optimum pH in the feed water to prevent corrosion of piping and equipment. Caustic soda (sodium hydroxide) is generally added for this purpose. Sometimes sodium carbonate is also added. Even though caustic soda is added with control, there are occasions when pH increases and cause corrosion as shown by the equation below. The damaged caused by excess alkali is because it dissolves the magnetite film forming sodium hypo ferrite and sodium ferrite both of which are soluble in hot concentrated caustic soda. In addition concentrated reacts directly and more rapidly with iron to form hydrogen and sodium Ferro rate.                       Fe3O4 + 4NaOH  ® 2 NaFeO2 + Na2FeO2 +H2O                       Fe + 2NaOH ®  Na2FeO2 Caustic attack on boiler can two forms  - Gouging or cracking. Caustic cracking is also known as caustic embrittlement. Caustic gouging  causes deep elliptical depression in boiler metal surface. This occur in areas of high heat flux or under heavy porous deposits. Underneath these deposits , boiler water can concentrate to the point where high concentrate of caustic can accumulate causing a localized corrosion. This action can be rapid. Boiler water chemistry if properly maintained will prevent caustic gouging. Caustic embrittlement or cracking is a form of stress corrosion. Cracks occur rapidly and are often undetectable leading to sudden failure of boiler –at times causing a violent failure. All parts of boiler are subjected to this type of corrosion. The only way  to stop this type of corrosion is to prevent high concentration from forming. Caustic corrosion is generally confined to a)      Water cooled tubes in region of high heat flux. b)      Slanted and horizontal tubes. c)       Location beneath heavy deposits. d)       Heat transfer region at or adjacent to packing rings. Caustic corrosion is prevented by coordinate caustic program. Phosphate ions act as a buffer ion. It does not allow pH to increase   in water, no matter how concentrated OH ions become. Buffer ions are also useful in avoiding similar high OH concentration which leads to stress corrosion cracking (caustic embrittlement). In low pressure boiler sodium nitrate is added in a definite ratio to caustic alkalinity to prevent caustic embrittlement. Galvanic corrosion We have already explained what galvanic corrosion is. A metal or alloy if it is electrically coupled, galvanic corrosion occurs. Corrosion by copper is the most common form of galvanic corrosion in boiler system. Copper can be carried from pre boiler section. Water deposits copper as decomposition of bicarbonates or as ammonia complexes. Pitting of boiler tubes has been reported due to copper deposit. Iron Oxide  deposits In boiler the steel reacts with water in absence of oxygen to form a magnetite film. This film than acts as a protective layer for further corrosion. Iron oxide also enters with feed water into boiler as corrosion product. This layer is very porous and can be easily penetrated. This allows boiler water to seep through and flash into steam leaving behind dissolved solids which concentrates in localized areas. This excessive concentration can lead to metal dissolution and metal failure.   Condensate corrosion   Steam generated in boiler is transported to point of use through pipes. Steam condensate is also returned  to boiler feed water. Corrosion of steam lines and condensate return line occurs because of the low pH. The chief source of acid in steam  is carbon di oxide. High temperature and pressure decomposes alkalinity to carbon di oxide, some of which dissolves in steam making it acidic. This lowers the condensate pH and leads to corrosion of return lines. Oxygen can enter a condensate system  from other sources even  if the deaerator is functioning properly. Oxygen causes a deep pitting of condensate lines.  High Velocity and low pH can result in extremely severe corrosion conditions. The best way to minimize this is by keeping the pH above 9.0 Other gases which can be corrosive in the condensate system are Ammonia, Hydrogen sulphide and sulphur di oxide.  Impure steam can create problems of carryover, priming and foaming in boiler. Steam gets contaminated because of the boiler water it carries with it or because of salt and silica which are, soluble in steam at high pressure. Solids carried over with steam can get deposited on super heater and turbine. Carryover can also effect the product quality.   Carryover Carryover is defined as contamination of steam with droplets of boiler water. Carry over can be due to entrainment  of water drops in steam  or due to property of certain salt like silica in boiler water to get vaporized and get into steam. The factors responsible for carry over are a)      Amount of dissolved solids in boiler water.  b)      Chemical nature of dissolve solids.  c)      Suspended solids in boiler water  d)      Boiler design  e)      Boiler operating condition  Many factors, both  mechanical and chemical contribute to carryover.  Mechanical Causes   Boiler design & operating conditions plays an important role in carryover. Without going into details we can say that major design & operating  factors responsible for carryover are : ·         Design pressure   ·         Steam drum size ·         Design generating rate   ·         Circulation rate. ·         Arrangement of down comers and risers   ·         Type of mechanical separating equipment. For example even when the TDS is within the limit, carryover can still occur because of change in operating condition. For example sudden increase in steam demand may lower the steam header pressure. This reduces drum pressure and water in the drum gets mixed with steam bubbles and the level rises. The rise in the drum level can cause carryover. Chemical Causes   Priming and foaming are two terms used with carryover. Priming is the surging of water in the steam outlet and is caused by factors like high water level in boiler, steaming rate, load fluctuations and boiler design. Priming is thus due to mechanical factors. Foaming is formation of stable bubbles. The bubbles don’t break because of  high surface tension .  Causes of foaming  are :  a. High Alkalinity : Caustic soda (NaOH) or sodium carbonate (Na2CO3) have     greater influence on foaming than neutral salts.  b. High TDS : High TDS  causes carryover. For a given boiler design and a given  set of  operating   condition There is a limiting  dissolved solid  content above which a serious steam contamination occurs. Reducing blow down by small amounts every few days  and measuring steam purity this limiting TDS value can be found out. This  value  is found by  keeping boiler operating conditions and other operating variables such as feed water   composition and treatment constant. If a graph is plotted between conductivity of  condensed steam  &  boiler water TDS the limiting figure is that corresponding to slightly  less than  where steam quality deteriorates. c. Suspended solids also cause foaming d. Oil is not present n boiler water. It can enter boiler system through leaks in condenser or other heat exchanger. Oil can also system because of lubrication of steam driven reciprocating equipment. Oil is undesirable in boiler for two reason (1) It acts as binder to form scale, (2) It also causes foaming. Even a very small amount can cause severe foaming and hence immediate action should be taken for complete removal of oil. e. Silica is another chemical which causes carryover. This is dealt separately. Silica All natural water contains silica. Like calcium and magnesium silica also forms scale. Removing silica from water is more difficult than removing Hardness (calcium and magnesium). At high temperature Silica volatizes and gets carried into steam and forms hard coating on turbine blades. Silica can form various kind of scale such as amorphous silica or magnesium Silicate. Amorphous silica scale forms like a glassy deposit which is very difficult to remove. Hydrofluoric acid is used to remove such scales. Silica scale is generally found in low pressure boiler because only softener is used and softener does not remove silica. Silica is not considered to be a big problem in low pressure boiler.

Closed systems usually contain a combination of different metals, which provide a high potential for galvanic corrosion. The potential for dissolved oxygen attach is generally quite low in closed systems because of small amount of makeup water the main oxygen source. However, in systems that require substantial makeup because of loss of water from leaks, oxygen is continually supplied and oxygen corrosion presents a serious problem. Oxygen can, at elevated temperatures or at point of high heat transfer, cause severe pitting corrosion.

Since relatively little makeup is added to most closed recirculating systems, it is practical and desirable to maintain the system in a corrosion -free condition. This is normally achieved by applying Chemicals Treatment at rather high concentrations.

Because water circulating through a closed system is not exposed to atmosphere, fouling by airborne silt and sand is rare. However, fouling by microbial masses may occur in closed systems where makeup rate is significant or process leaks encourage bacterial growths. These are controlled with biological control agents formulated to be compatible with the Chemical Treatments and operating conditions found in closed systems.

Scale should be a minor problem in a closed system since the water is not concentrated by evaporation. In a tightly closed system, none of the common scale-forming constituents deposit on metal surfaces to interfere with heat transfer or encourage corrosion.

With high make up rates, however, additional scale forms with each new increment of water added so that in time, scale becomes significant. In addition, there is opportunity for sludge, rust, and suspended solids to drop out at low flow points and bake on heat transfer surfaces to form a hard deposit. Therefore, scale retardants and dispersants are usually included as part of closed system Chemical Treatment program where makeup rates are high. Often soft water or condensate is used for make to closed systems depending on the characteristics of the system being protected.

For a successful Chiller Water Treatment, it is requires regular analysis for control of correct Treatment Chemical Residuals.