US2046308A - Boiler water conditioning - Google Patents

Boiler water conditioning Download PDF

Info

Publication number
US2046308A
US2046308A US25696A US2569635A US2046308A US 2046308 A US2046308 A US 2046308A US 25696 A US25696 A US 25696A US 2569635 A US2569635 A US 2569635A US 2046308 A US2046308 A US 2046308A
Authority
US
United States
Prior art keywords
boiler
water
phosphite
ammonium
phosphate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US25696A
Inventor
Cyrus W Rice
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US25696A priority Critical patent/US2046308A/en
Application granted granted Critical
Publication of US2046308A publication Critical patent/US2046308A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/20Treatment of water, waste water, or sewage by degassing, i.e. liberation of dissolved gases

Definitions

  • sodium phosphite NazHPOa
  • acid sodium phosphite NaHzPOs
  • sodium hypophospnite NazHzPzos
  • potassium phosphite K2HPO3
  • potassium hypophosphite KHzPOz
  • ammonium phosphite NH4H2PO3
  • ammonium hypophosphite NH4H2PO2
  • the phosphite may be added in appropriate quantity to the boiler feed water, and is carried to the boiler.
  • the phosphite molecules In solution in the feedwater, and/or in the boiler concentrate, the phosphite molecules each take up oxygen to pass into the form of the appropriate phosphate. In the presence in the boiler of an adequate excess of the basic radical, it also passes into the tribasicform.
  • ammonia goes over with the steam
  • ammonia reacts with any contained carbon dioxide to produce ammonium carbonate.
  • ammonia carried over with the steam prevents carbon dioxide corrosion, as may be illus- V trated by the following formula:
  • a soluble phosphite added to the boiler feed water deoxidizes the water, thus fully performing the reducing function previously performed by sodium sulphite, and incidentally exhibiting an increased deoxidizing activity as compared with that compound; it further performs the additional function of inhibiting boiler encrustation, by reaction with calcium and magnesium, in its progressive activity in the boiler. If a phosphite of ammonium be used, the third function, attributable to ammonia, of inhibiting carbon dioxide corrosion by the steam passing from the boiler is obtained.
  • any adequate water-soluble phosphite is capable of performing both the function of removing oxygen from the boiler water, and the function of forming a phosphate reactive with the encrustation forming substances, calcium and magnesium.
  • the secondary effect obtained by adding a water-soluble phosphite to the boiler feed water, and the tertiary effect of adding ammonium phosphite to the boiler feed water, is dependent upon the presence of oxygen content in the water adequate to efiect saturation of the phosphite. If, then, the water has initially a notably low oxygen content, it may be desirable to introduce into the boiler a watersoluble phosphate in order that the encrustation inhibiting reaction may be complete, or to lessen the calcium and magnesium content, by appropriate treatment of the boiler feed Water.
  • the method herein described of conditioning boiler water and steam generated therefrom which comprises deoxidizing the water by the reducing action of ammonium phosphite thereon, by sequential reactions of the phosphate produced by oxidation in the boiler water removing from the water the encrustation forming con tent thereof, and in the sequential reactions of the phosphate produced by oxidation of ammonium phosphite liberating ammonia to pass from the boiler with steam generated in the boiler.

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Gas Separation By Absorption (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Description

PTE
(il FlCE BOEER WATER CONDITIONING Cyrus W. Rice, Ifittsburgh, Pa.
No Drawing. Application June 8, 1935,
Serial No. 25,696
'1 Claim. I (Cl. 2210-23) This invention relates to boiler'water treatment.
In use of a steam generating boiler it is of importance that the water introduced to the boiler be freed, or substantially freed, of dissolved oxygen prior to its introduction. This is for the reason that oxygen in the boiler water is an active adjunct to boiler corrosion. It is also of importance that in the boiler there be maintained favorable conditions of such nature as to inhibit the formation of encrustations on the inner surface of the boiler wall.
I have succeeded in inhibiting both oxygen produced boiler corrosion and boiler encrustation by introducing into the boiler feed water a water soluble phosphite. 'As dissolved in the boiler feed water, phosphite performs the dual function of reducing agent and encrustation inhibiting a ent.
The phosphites of the alkali metals, sodium,
potassium, and ammonium are all suitablefor my purpose, 'all being adequately water soluble. Thus I have found advantageously usable disodium phosphite (NazHPOa); acid sodium phosphite (NaHzPOs) sodium hypophospnite (NazHzPzos); potassium phosphite (K2HPO3); potassium hypophosphite (KHzPOz); ammonium phosphite (NH4H2PO3); and ammonium hypophosphite (NH4H2PO2).
In each instance the phosphite may be added in appropriate quantity to the boiler feed water, and is carried to the boiler. In solution in the feedwater, and/or in the boiler concentrate, the phosphite molecules each take up oxygen to pass into the form of the appropriate phosphate. In the presence in the boiler of an adequate excess of the basic radical, it also passes into the tribasicform.
As all well conditioned boiler concentrates carries more or less sodium hydroxide, or its equivalent,-there will normally be maintained in the water an excess of sodium radical, or potassium radical. If, therefore, a sodium or potassium phosphite be used, there is normally present in the boiler a sufficiency of the appropriate radical to produce the tribasic phosphate.
Thereactions involved are thus, for example:
Under boiler conditions, therefore, the initial sodium or potassium phosphite, in performing the useful function of deoxidation, is converted into' a phosphate reactive with compounds of calcium and magnesium. These latter are the agencies producing boiler encrustation, as they may exist in the boiler in the form of calcium or magnesium sulphate or carbonate. To give a typical reaction for this effect, trisodium phosphate (NEiBPO) reacts both with calcium sulphate (Ca/3504) and calcium carbonate (CazHCOa) as follows:
The reactions with the compounds of magnesium normally present in the boiler water are identical.
Of the products of reaction, calcium phosphate We thus have, from the addition of ammonium phosphite also, an inclusion of the trisodium phosphate in the boiler. water. As above explained, and illustrated, this secondary product of reaction reacts with the compounds of calcium and magnesium normally present to produce the sludge forming calciumphosphate and magnesium phosphate.
The ammonia (NHa) goes over with the steam,
and performs a conditioning effect thereon. In any condensate of the steam, as it occurs in lines,
cylinders, turbines, or the like, the ammonia reacts with any contained carbon dioxide to produce ammonium carbonate. In this manner 5 the ammonia carried over with the steam prevents carbon dioxide corrosion, as may be illus- V trated by the following formula:
2NH3+COz+H2O- (NH4)2C O3 The advantages attending the use of a. potassium phosphite are identical with those obtained A by the use of a sodium phosphite. The specific advantage attendant upon the production of ammonia in the boiler is, therefore, that it is carried over with the steam, and is thus enabled to nullify'the corrosive tendency of carbon dioxide in any connections and equipment to which the steam passes. For this reason I prefer to utilize a phosphite of ammonium.
To summarize: a soluble phosphite added to the boiler feed water deoxidizes the water, thus fully performing the reducing function previously performed by sodium sulphite, and incidentally exhibiting an increased deoxidizing activity as compared with that compound; it further performs the additional function of inhibiting boiler encrustation, by reaction with calcium and magnesium, in its progressive activity in the boiler. If a phosphite of ammonium be used, the third function, attributable to ammonia, of inhibiting carbon dioxide corrosion by the steam passing from the boiler is obtained.
While I have disclosed as peculiarly suitable the phosphites of sodium, potassium, and ammonium, I do not intend to limit the scope of I my invention to the utilization of the phosphites of these alkali metals. Any adequate water-soluble phosphite is capable of performing both the function of removing oxygen from the boiler water, and the function of forming a phosphate reactive with the encrustation forming substances, calcium and magnesium.
On the quantitative side, the secondary effect obtained by adding a water-soluble phosphite to the boiler feed water, and the tertiary effect of adding ammonium phosphite to the boiler feed water, is dependent upon the presence of oxygen content in the water adequate to efiect saturation of the phosphite. If, then, the water has initially a notably low oxygen content, it may be desirable to introduce into the boiler a watersoluble phosphate in order that the encrustation inhibiting reaction may be complete, or to lessen the calcium and magnesium content, by appropriate treatment of the boiler feed Water. It cannot be considered, however, that occasional initial preponderance of calcium and magnesium content over oxygen content in the boiler Water detracts from the sequential completeness of the favorable result obtained by the use of phosphite. It will. be understood from the above that the phosphite employed should be added to the feed,
water in combining proportion with the determined oxygen content of the water available for use in the boiler.
I claim as my invention:
The method herein described of conditioning boiler water and steam generated therefrom which comprises deoxidizing the water by the reducing action of ammonium phosphite thereon, by sequential reactions of the phosphate produced by oxidation in the boiler water removing from the water the encrustation forming con tent thereof, and in the sequential reactions of the phosphate produced by oxidation of ammonium phosphite liberating ammonia to pass from the boiler with steam generated in the boiler.
CYRUS WM. RICE.
US25696A 1935-06-08 1935-06-08 Boiler water conditioning Expired - Lifetime US2046308A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US25696A US2046308A (en) 1935-06-08 1935-06-08 Boiler water conditioning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US25696A US2046308A (en) 1935-06-08 1935-06-08 Boiler water conditioning

Publications (1)

Publication Number Publication Date
US2046308A true US2046308A (en) 1936-06-30

Family

ID=21827565

Family Applications (1)

Application Number Title Priority Date Filing Date
US25696A Expired - Lifetime US2046308A (en) 1935-06-08 1935-06-08 Boiler water conditioning

Country Status (1)

Country Link
US (1) US2046308A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2476598A (en) * 1945-02-16 1949-07-19 Hall Lab Inc Treatment of steam boiler water
US2562571A (en) * 1945-05-30 1951-07-31 Hall Lab Inc Treatment of steam systems
US2627502A (en) * 1949-05-07 1953-02-03 Nat Aluminate Corp Boiler water treatment
DE767910C (en) * 1939-05-20 1954-10-04 Ig Farbenindustrie Ag Prevents condensation from attacking iron materials

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE767910C (en) * 1939-05-20 1954-10-04 Ig Farbenindustrie Ag Prevents condensation from attacking iron materials
US2476598A (en) * 1945-02-16 1949-07-19 Hall Lab Inc Treatment of steam boiler water
US2562571A (en) * 1945-05-30 1951-07-31 Hall Lab Inc Treatment of steam systems
US2627502A (en) * 1949-05-07 1953-02-03 Nat Aluminate Corp Boiler water treatment

Similar Documents

Publication Publication Date Title
US1903041A (en) Water treatment
DE1045373B (en) Use of phosphonic acids
US2046308A (en) Boiler water conditioning
US2505457A (en) Method of inhibiting scale
US2576386A (en) Inhibition of scale formation in steam generation
US2627502A (en) Boiler water treatment
US1930885A (en) Process for the treatment of hard waters
Beeson et al. Preparation of Physiologically Neutral Fertilizer Mixtures-Reactions of Monoammonium Phosphate with Limestone and with Dolomite
US2360730A (en) Process of treating water for steam boilers
US2675351A (en) Method for preventing corrosion and scale
GB316136A (en) Manufacture of crystalline phosphates
EP0237775A2 (en) Stable ammonium Polyphosphate liquid fertilizer from merchant grade phosphoric acid
US1857571A (en) Process for reacting acid phosphates with ammonia liquor
US1372051A (en) Process for the manufacture of phosphatic fertilizer
US1002143A (en) Process of producing calcium metaphosphate and ammonia.
US1260740A (en) Treatment of iron and steel to prevent corrosion.
DE429767C (en) Process to increase the production and the phosphoric acid content of the Thomas slag
US1835441A (en) Process for producing tri-ammonium phosphate
SU66676A1 (en) Method of protection against corrosion by the action of mineral acids
AT62216B (en) Process for the simultaneous production of ammonium phosphate and ammonium nitrate.
EP1819845A1 (en) Cleaning method for removing deposits containing magnetite out of a pressure vessel of a power plant
Hough Titration of Fer [UNK] rous Salts in the Presence of Hydrochloric and Phosphoric Acids.
US1360401A (en) Fertilizer and process for making the same
GB190925082A (en) Improvements in the Method and Process of Treating Salt and Bye-products.
SU46250A1 (en) Method for producing hydrogen from water vapor