US2995477A - Boiler cleaning process - Google Patents

Boiler cleaning process Download PDF

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Publication number
US2995477A
US2995477A US511392A US51139255A US2995477A US 2995477 A US2995477 A US 2995477A US 511392 A US511392 A US 511392A US 51139255 A US51139255 A US 51139255A US 2995477 A US2995477 A US 2995477A
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Prior art keywords
boilers
cleaning
water
boiler
acid
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US511392A
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Albert G Florence
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Celanese Corp
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Celanese Corp
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Priority to US511392A priority Critical patent/US2995477A/en
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F5/00Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
    • C02F5/08Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
    • C02F5/10Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/02Cleaning or pickling metallic material with solutions or molten salts with acid solutions
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28GCLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
    • F28G9/00Cleaning by flushing or washing, e.g. with chemical solvents

Definitions

  • This invention relates to a cleaning process and relates more particularly to a process for cleaning boilers and other types of equipment wherein water is heated or cooled.
  • boilers In the operation of boilers and other types of equipment wherein water is heated or cooled, hereinafter referred to collectively as boilers, there is a tendency for scale to deposit on the surfacesof said boilers with which the water, in either liquid or vapor form. comes into contact. As the scale accumulates on the boiler surfaces it reduces the efliciency with which heat is transferred through the said surfaces so that it is necessary to clean the said surfaces fromv time to time in order to maintain the efficiency of the boiler at a reasonably high level.
  • One of the methods that has been suggested for cleaning the boilers is to introduce a strong mineral acid, such as hydrochloric or sulfuric acid, into the boilers to react with the scale, usually in an amount equal in weight to the weight of the scale.
  • Corrosion inhibitors are added to the boilers together with the mineral acids to minimize attack by the mineral acids on the boiler surfaces themselves.
  • the danger is ever present that the mineral acids will attack the boiler surfaces despite the presence of corrosion inhibitors.
  • the use of mineral acids involves a considerable inconvenience owing to the precautions that must be taken to insure safety during the handling and application of the same.
  • a further object of this invention is to provide a process for cleaning boilers by introducing an organic acid into the water contained in said boilers to bring the pH of said water to a predetermined level.
  • boilers are cleaned by adding to the water present in said boilers an organic acid in an amount sufficient to bring the pH of said water to a value of between about 3 and 5.
  • the water in said boilers is held at an elevated temperature until the scale is removed from the boiler surfaces, after which the boilers are drained and washed.
  • acetic acid as the treating acid owing to its ready availability and low cost and the good results obtained therewith.
  • other acids may also be employed such as, for example, formic, propionic, benzoic, butyric, fumaric, malonic, phthalic, and oxalic or mixtures of the said-acids.
  • the quantity of acid added to the water in the boiler should be sufficient to bring the pH thereof to between about 3 and 5, or preferably to between about 3 and 4.
  • the acid is introduced into the boiler system slowly so as to avoid the presence in localized parts of the system of high concentrations of acid which will bring the pH of the water in such localized parts to a value much below the lower limit specified above since, in this case, the danger may arise that the acid will attack the boiler surfaces.
  • the water to which the organic acid is added is held at an elevated temperature for a period of time sufficient to remove the scale therefrom.
  • the precise temperature of treatment is not critical and may be as high as the normal operating temperature of the boiler which may range as high as 210 C., or even higher, or the treating temperature may be as low as C., or even less.
  • the time of treatment should be sufficient to remove substantially all the scale from the boiler and will depend on the nature and thickness of the scale, the precise pH of treatment, and the temperature of treatment. For any given boiler and set of conditions, such time may be readily ascertained by a simple trial.
  • the boiler is heavily blown down by hand periodically (every three to four hours). At the completion of this operating period, the boiler is brought down and thoroughly washed again and is found to be thoroughly clean and free of scale.
  • Process for cleaning boilers which comprises introducing acetic acid into the water contained in said boilers to bring the pH thereof to between about 3 and 4, the rate of introduction of the acetic acid being such that the pH does not fall below the values specified in any localized portions of the boiler system, and holding the water in said boilers at a temperature of about 100 to 210 C. until the cleaning has been carried out.
  • Process for cleaning scaly boilers which comprises introducing an organic acid into the water contained in said scaly boilers to bring the pH thereof to between about 3 and 5, and holding the water in said boilers at an elevated temperature of at least about 100 C. until the cleaning has been carried out.
  • Process for cleaning scaly boilers which comprises introducing an organic acid into the water contained in said scaly boilers to reduce the pH thereof to between about 3 and 5, the rate of introduction of the organic acid being such that the pH does not fall below the values specified in any localized portions of the boiler system,
  • Process for cleaning scaly boilers which comprises introducing acetic acid into the water contained in said scaly boilers to bring the pH thereof to between about 3 and 5, and keeping the water in said boilers hot until the cleaning has been carried out.
  • Process for cleaning boilers which comprises introducing acetic acid into the water contained in said boilers to bring the pH thereof to between about 3 and 5, the rate of introduction of the acetic acid being such that .the pH does not fall below the values specified in any least about 100 C. until the cleaning has been carried out.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)

Description

7 2,995,477 BOILER CLEANING PROCESS Albert G. Florence, Kingsville, Tex., asslgnor to Celanese Corporation of America, New York, N.Y., a corporation of Delaware No Drawing. Filed May 26, 1955, Ser. No. 511,392 Claims. (Cl. 134-22) This invention relates to a cleaning process and relates more particularly to a process for cleaning boilers and other types of equipment wherein water is heated or cooled.
In the operation of boilers and other types of equipment wherein water is heated or cooled, hereinafter referred to collectively as boilers, there is a tendency for scale to deposit on the surfacesof said boilers with which the water, in either liquid or vapor form. comes into contact. As the scale accumulates on the boiler surfaces it reduces the efliciency with which heat is transferred through the said surfaces so that it is necessary to clean the said surfaces fromv time to time in order to maintain the efficiency of the boiler at a reasonably high level. One of the methods that has been suggested for cleaning the boilers is to introduce a strong mineral acid, such as hydrochloric or sulfuric acid, into the boilers to react with the scale, usually in an amount equal in weight to the weight of the scale. Corrosion inhibitors are added to the boilers together with the mineral acids to minimize attack by the mineral acids on the boiler surfaces themselves. However, the danger is ever present that the mineral acids will attack the boiler surfaces despite the presence of corrosion inhibitors. Moreover, the use of mineral acids involves a considerable inconvenience owing to the precautions that must be taken to insure safety during the handling and application of the same.
It is an important object of this invention to provide a process for cleaning boilers which will be free from the foregoing and other disadvantages.
A further object of this invention is to provide a process for cleaning boilers by introducing an organic acid into the water contained in said boilers to bring the pH of said water to a predetermined level.
Other objects of this invention will be apparent from the following detailed description and claims.
According to the present invention, boilers are cleaned by adding to the water present in said boilers an organic acid in an amount sufficient to bring the pH of said water to a value of between about 3 and 5. The water in said boilers is held at an elevated temperature until the scale is removed from the boiler surfaces, after which the boilers are drained and washed. Through the use i United States Patent 0 In carrying out the present invention, it is preferred to employ acetic acid as the treating acid owing to its ready availability and low cost and the good results obtained therewith. However, other acids may also be employed such as, for example, formic, propionic, benzoic, butyric, fumaric, malonic, phthalic, and oxalic or mixtures of the said-acids. The quantity of acid added to the water in the boiler should be sufficient to bring the pH thereof to between about 3 and 5, or preferably to between about 3 and 4. Advantageously, the acid is introduced into the boiler system slowly so as to avoid the presence in localized parts of the system of high concentrations of acid which will bring the pH of the water in such localized parts to a value much below the lower limit specified above since, in this case, the danger may arise that the acid will attack the boiler surfaces.
Patented Aug. 8, 1961 While there is little or no danger that-the organic acids in the concentrations specified will attack the bo ler surfaces, so that it is not essential to employ a corrosion inhibitor therewith, it .may be desirable in certain cases v however, there should be employed between about 10 and 200 ppm. of the inhibitor based on water present.
The water to which the organic acid is added is held at an elevated temperature for a period of time sufficient to remove the scale therefrom. The precise temperature of treatment is not critical and may be as high as the normal operating temperature of the boiler which may range as high as 210 C., or even higher, or the treating temperature may be as low as C., or even less. The time of treatment should be sufficient to remove substantially all the scale from the boiler and will depend on the nature and thickness of the scale, the precise pH of treatment, and the temperature of treatment. For any given boiler and set of conditions, such time may be readily ascertained by a simple trial.
The following example is given to illustrate this invention further:
Example .the mud drum of said boiler over a twenty-four hour period. Rate of acid-inhibitor feed is that necessary to maintain a pH of between 3.7 and 4.0. The boiler is heavily blown down by hand periodically (every three to four hours). At the completion of this operating period, the boiler is brought down and thoroughly washed again and is found to be thoroughly clean and free of scale.
It is to be understood that the foregoing detailed description is merely given by way of illustration and that many variations may be made therein without departing from the spirit of my invention.
Having described my invention, what I desire to secure by Letters Patent is:
1. Process for cleaning boilers which comprises introducing acetic acid into the water contained in said boilers to bring the pH thereof to between about 3 and 4, the rate of introduction of the acetic acid being such that the pH does not fall below the values specified in any localized portions of the boiler system, and holding the water in said boilers at a temperature of about 100 to 210 C. until the cleaning has been carried out.
2. Process for cleaning scaly boilers which comprises introducing an organic acid into the water contained in said scaly boilers to bring the pH thereof to between about 3 and 5, and holding the water in said boilers at an elevated temperature of at least about 100 C. until the cleaning has been carried out.
3. Process for cleaning scaly boilers which comprises introducing an organic acid into the water contained in said scaly boilers to reduce the pH thereof to between about 3 and 5, the rate of introduction of the organic acid being such that the pH does not fall below the values specified in any localized portions of the boiler system,
The amount of inhibitor that will be and keeping the water in said boilers hot until the cleaning has been carried out.
4. Process for cleaning scaly boilers which comprises introducing acetic acid into the water contained in said scaly boilers to bring the pH thereof to between about 3 and 5, and keeping the water in said boilers hot until the cleaning has been carried out.
5. Process for cleaning boilers which comprises introducing acetic acid into the water contained in said boilers to bring the pH thereof to between about 3 and 5, the rate of introduction of the acetic acid being such that .the pH does not fall below the values specified in any least about 100 C. until the cleaning has been carried out.
References (Jited in the file of this patent UNITED STATES PATENTS 1,135,684 Greenhorne'" Apr. 13, 1915 1,892,093 Battistella Dec. 27, 1932 2,524,757 Brines "a Oct. 10, 1950 FOREIGN PATENTS 248,886 Great Britain Mar. 28, 1926 OTHER REFERENCES Britton: Hydrogen Ions, page 48, D. Van Nostrand (30., Inc., New York, 1929.

Claims (1)

  1. 2. PROCESS FOR CLEANING SCALY BOILERS WHICH COMPRISES INTRODUCING AN ORGANIC ACID INTO THE WATER CONTAINED IN SAID SCALY BOILERS TO BRING THE PH THEREOF TO BETWEEN ABOUT 3 AND 5, AND HOLDING THE WATER IN SAID BOILERS AT AN ELEVATED TEMPERATURE OF AT LEAST ABOUT 100*C. UNTIL THE CLEANING HAS BEEN CARRIED OUT.
US511392A 1955-05-26 1955-05-26 Boiler cleaning process Expired - Lifetime US2995477A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3072502A (en) * 1961-02-14 1963-01-08 Pfizer & Co C Process for removing copper-containing iron oxide scale from metal surfaces
US3277008A (en) * 1962-04-20 1966-10-04 Pfaudler Permutit Inc Surface cleaning method and composition
US3298931A (en) * 1962-01-15 1967-01-17 Commw Scient Ind Res Org Removal of scale in distillation of sea water containing magnesium salts
US4855069A (en) * 1986-01-31 1989-08-08 Rhone-Poulenc Chimie Polysaccharide-thickened aqueous acid cleaning compositions
US5542981A (en) * 1994-06-22 1996-08-06 Lee, Sr.; Clel E. Process for removing mineral deposits from lagoon recycle lines
US20060141408A1 (en) * 2004-12-17 2006-06-29 Clyde Bergemann Gmbh Method and apparatus for removing combustion residues using different cleaning media

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1135684A (en) * 1913-09-26 1915-04-13 Thomas Ritchie Greenhorne Process for removing scale from incrusted surfaces.
GB248886A (en) * 1925-01-28 1926-03-18 Alfred Andrew Cozens Process for the softening or breaking down of hard calcareous and like materials, such as water-laid deposits and incrustations
US1892093A (en) * 1932-12-27 Method of removing rust
US2524757A (en) * 1945-05-17 1950-10-10 Dow Chemical Co Cleaning scaled vessels

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1892093A (en) * 1932-12-27 Method of removing rust
US1135684A (en) * 1913-09-26 1915-04-13 Thomas Ritchie Greenhorne Process for removing scale from incrusted surfaces.
GB248886A (en) * 1925-01-28 1926-03-18 Alfred Andrew Cozens Process for the softening or breaking down of hard calcareous and like materials, such as water-laid deposits and incrustations
US2524757A (en) * 1945-05-17 1950-10-10 Dow Chemical Co Cleaning scaled vessels

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3072502A (en) * 1961-02-14 1963-01-08 Pfizer & Co C Process for removing copper-containing iron oxide scale from metal surfaces
US3298931A (en) * 1962-01-15 1967-01-17 Commw Scient Ind Res Org Removal of scale in distillation of sea water containing magnesium salts
US3277008A (en) * 1962-04-20 1966-10-04 Pfaudler Permutit Inc Surface cleaning method and composition
US4855069A (en) * 1986-01-31 1989-08-08 Rhone-Poulenc Chimie Polysaccharide-thickened aqueous acid cleaning compositions
US5542981A (en) * 1994-06-22 1996-08-06 Lee, Sr.; Clel E. Process for removing mineral deposits from lagoon recycle lines
US20060141408A1 (en) * 2004-12-17 2006-06-29 Clyde Bergemann Gmbh Method and apparatus for removing combustion residues using different cleaning media
US7767027B2 (en) * 2004-12-17 2010-08-03 Clyde Bergemann Gmbh Method and apparatus for removing combustion residues using different cleaning media

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