US691324A - Pigment and the production thereof from ferrous liquors. - Google Patents

Pigment and the production thereof from ferrous liquors. Download PDF

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US691324A
US691324A US2947700A US1900029477A US691324A US 691324 A US691324 A US 691324A US 2947700 A US2947700 A US 2947700A US 1900029477 A US1900029477 A US 1900029477A US 691324 A US691324 A US 691324A
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ferrous
liquor
sulfate
basic ferric
tank
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US2947700A
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Alexander Sydney Ramage
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ELMER A SPERRY
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ELMER A SPERRY
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/04Obtaining nickel or cobalt by wet processes
    • C22B23/0453Treatment or purification of solutions, e.g. obtained by leaching
    • C22B23/0461Treatment or purification of solutions, e.g. obtained by leaching by chemical methods
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S423/00Chemistry of inorganic compounds
    • Y10S423/01Waste acid containing iron
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S423/00Chemistry of inorganic compounds
    • Y10S423/01Waste acid containing iron
    • Y10S423/02Sulfuric acid

Definitions

  • My invention relates to a new and improved process for the utilization of ferrous liquors, especially Waste iron-pickle liquor.
  • the object of my invention is to obtain a new chemical compound of great value in the arts, principally as a coloring material or pigment or as a base for such material.
  • My invention consists in treating ferrous liquor in the manner hereinafter set forth, producing thereby a hydrated basic ferric oxid having the composition Fe O Fe (OH)
  • This pickle liquor is usually composed of ferrous sulfate or ferrous-chlorid and may contain a small percentage of free acid. Some of these liquors are already utilized to some extent in the production of copperas variously used in the arts and from which is produced Venetian red, iron oxid, &c.
  • I My process consists, in general, in'oxidizing the ferrous liquor preferably by blowing through it air or air and steam finely divided and adding to the body of the ferrous liquor at any suitable time-as, for instance, during the process of oxidizing-an alkaline materialfor example, a solution containing an alkaline-earth carbonate'to the point approximating neutrality and a comparatively large quantity of water, or the water may have been previously added in an amount at least equal in bulk to twice the original bulk of the ferrous liquor.
  • oxidizing-an alkaline material for example, a solution containing an alkaline-earth carbonate'to the point approximating neutrality and a comparatively large quantity of water, or the water may have been previously added in an amount at least equal in bulk to twice the original bulk of the ferrous liquor.
  • the accompanying drawing illustrates apparatus suitable for carrying out my invention, in which 1) represents a tank adapted to v tank I) to be sixteen feet deep and seven feet in diameter. If the ferrous liquor has a strength of 28-Baum, the liquor is run into the tank 17 to the depth of four feet, and this quantity of liquor will practically contain four thousand five hundred pounds of copperas, (FeSO ,7H O.) Should the liquor be of another strength, such as 1 F Baum, then the liquor is run into the tank to a depth of eight feet, and in similar proportion according to the strength of the liquor, so that the quantity of liquor taken into the tank at any time shall contain approximately four thousand five hundred pounds copperas.
  • the tank a is provided with an agitator Z and is also provided with a pipe at for conducting the contents of the tank a into the tank I).
  • the pipe at is preferably provided with a valve 0 3.
  • 0 represents a closed tank located, preferably, below the level of the tank 6, into which the contents of tank I) drains through the pipe 1), which is provided with a valve b 9 represents an air-p u mp for creating an airpressure in the tank 0.
  • a pipe 0 leads from the tank 0 to the filter d.
  • 7c represents a water-supply pipe for sup- I plying water to the tank I).
  • carbonate of soda carbonate of magnesia instead of the solution of carbonate of soda carbonate of magnesia, carbonate of calcium, or carbonate of bariumvmay be used.
  • water preferably at a boiling temperature, may be introduced through the supply-pipe k in such quantity that the bulk of the added water will preferably at least equal twice the original bulk of the ferrous liquor. This is on the presumption that 28 Baum liquor hasbeen used. Shouldaweaker liquor be used, the bulk of theadded water must be such that at the close of the operation the contents of the tank will stand twelve feet deep or over. In other words, the dilution of the liquor must be in such proportion that at the close of the operation the liquid will stand in a tank of the given dimensions to about the depth of twelve feet when four thousand five hundred pounds of copperas has been taken.
  • Basic ferric sulfate formed by blowing the ferrous liquor is an example of the first class above mentioned and is therefore on the addition of sufficient water resolved into sulfuric acid and basic ferric hydrate.
  • the acid is neutralized and set free by the gradual addition of sodium or other carbonate, thereby preventing the reaction from reaching an equilibrium and determining the complete decomposition of the basic ferric sulfate. It will thus be seen that the added water is the active precipitating agent and that the reaction is effected by hydrolysis.
  • the liquor after being treated in the tank bis run into the tank 0, from which it is forced by air -pressure through the pipe 0' into the filter d.
  • the sulfate or chlorid solution runs 01?, and the hydrated basic ferric oxid which remains as a filtrate is collected and washed and dried at a low heat.
  • the hydrated basic ferric oxid can be dried in its original state or calcined to produce the various shades of iron-oxid reds.
  • the calcination will require little furnacing, producing shadestsurpassing. those produced by the calcination of copperas and giving also an oxid which requires no levigation or grinding, being in a very fine state of subdivision and having no trace of acid or undecomposed sulfate.
  • My process is equally adapted to the treatment of either a ferrous-sulfate or a ferrouschlorid liquor.
  • an alkaline carbonate used in carrying out my process the basic ferric oxid is obtained purer, as the snlfatesand chlorids of alkalies remain in solution.
  • ferrous-chlorid liquor be treated with an alkaline-earth carbonate-such as barium, calcium, or strontium-then chlorids of these metals are obtained in solution and the pure basic ferric oxid is precipitated.
  • the resulting liquor can be evaporated and utilized in the usual way or may be used for making blanc fixe in case a carbonate of barium has been employed or pearl-hardening if calcium-carbonate has been employed.
  • ferrous-sulfate liquor is treated with an alkaline-earth carbonate, the basic ferric basic ferric hydrate.
  • the light ferric hydrate having the formula the same being of a golden-yellow color, suitable for pigment,fine and velvety to the touch, absorbing more oil than standard French ocher, zinc-white or white lead, and also having more covering power than these pigments.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Iron (AREA)

Description

N0. 69l,324. Patented Jan. I4, I902.
A. S. RAMAGE.
PIGMENT AND THE PRUDUCTION THEREOF FROM FERBOUS LIQUORS.
(Application filed tse n. 1o,- 190D.)
(No Model.)
WI TNBSEES INYENTUH' LQQMLJE Q BY I 5' 3 Ty: "cams pzrcns co.. uofauwa. WASHINGTON. u. c.
UNITED STATES.
PATENT OFFICE.
ALEXANDER SYDNEY RAMAGE, OF CLEVELAND, OHIO, ASSIGNOR,
BY DIRECT'AND MESNE ASSIGNMENTS, TO ELMER A. SPERRY,
OF CLEVELAND, OHIO.
PIGMENT AND THE PRODUCTION THEREOF FROM FERROUS LIQUORS.
SIECIFICATION forming part of Letters Patent No. dated'January 1902- Application filed September 10, 1900. Serial No. 29,477- tNo'srecimensJ 1'0 aZZ whom, it may concern.-
Be it known that I, ALEXANDER SYDNEY RAMAGE, a resident of Cleveland, in the county of Ouyahoga and State of Ohio, have invented certain new and useful Improvements in Processes for the Utilization of Ferrous Liquors; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it pertains to make and use the same.
My invention relates to a new and improved process for the utilization of ferrous liquors, especially Waste iron-pickle liquor.
The object of my invention is to obtain a new chemical compound of great value in the arts, principally as a coloring material or pigment or as a base for such material.
- My invention consists in treating ferrous liquor in the manner hereinafter set forth, producing thereby a hydrated basic ferric oxid having the composition Fe O Fe (OH) The ferrousliquor which I propose utilizing in carrying out my invention is usually a waste product remaining after the pickling of iron and is obtainable in large quantities from wire =works, galvanizing-Works, ironplate works, and similar manufactories, or
such liquor may be compounded in any suitable manner. This pickle liquor is usually composed of ferrous sulfate or ferrous-chlorid and may contain a small percentage of free acid. Some of these liquors are already utilized to some extent in the production of copperas variously used in the arts and from which is produced Venetian red, iron oxid, &c. I My process consists, in general, in'oxidizing the ferrous liquor preferably by blowing through it air or air and steam finely divided and adding to the body of the ferrous liquor at any suitable time-as, for instance, during the process of oxidizing-an alkaline materialfor example, a solution containing an alkaline-earth carbonate'to the point approximating neutrality and a comparatively large quantity of water, or the water may have been previously added in an amount at least equal in bulk to twice the original bulk of the ferrous liquor.
The accompanying drawing illustrates apparatus suitable for carrying out my invention, in which 1) represents a tank adapted to v tank I) to be sixteen feet deep and seven feet in diameter. If the ferrous liquor has a strength of 28-Baum, the liquor is run into the tank 17 to the depth of four feet, and this quantity of liquor will practically contain four thousand five hundred pounds of copperas, (FeSO ,7H O.) Should the liquor be of another strength, such as 1 F Baum, then the liquor is run into the tank to a depth of eight feet, and in similar proportion according to the strength of the liquor, so that the quantity of liquor taken into the tank at any time shall contain approximately four thousand five hundred pounds copperas.
The tank a is provided with an agitator Z and is also provided with a pipe at for conducting the contents of the tank a into the tank I). The pipe at is preferably provided with a valve 0 3.
0 represents a closed tank located, preferably, below the level of the tank 6, into which the contents of tank I) drains through the pipe 1), which is provided with a valve b 9 represents an air-p u mp for creating an airpressure in the tank 0. A pipe 0 leads from the tank 0 to the filter d.
7c represents a water-supply pipe for sup- I plying water to the tank I).
In carrying out my process I proceed as follows: The ferrous liquor is collected in asuitable tank, in which any free acid should first be neutralized. It is then led to the tank or converter 19. Air or air and .steam finely divided are preferably admitted to the pipe h through the pipes f and h, respectively, and the mixture is forced under pressure through the perforations 7L into the body of the liquor, thoroughly oxidizing the same. As the oxidation of the ferrous liquor proceeds a substance or solution of a suitable alkaline reaction, preferably carbonate of soda, which has been previously placed in the tank a, is run into the ferrous liquor to the approximate point of neutrality. Instead of the solution of carbonate of soda carbonate of magnesia, carbonate of calcium, or carbonate of bariumvmay be used. At the same time that the carbonate of soda is being added to the ferrous liquor, water, preferably at a boiling temperature, may be introduced through the supply-pipe k in such quantity that the bulk of the added water will preferably at least equal twice the original bulk of the ferrous liquor. This is on the presumption that 28 Baum liquor hasbeen used. Shouldaweaker liquor be used, the bulk of theadded water must be such that at the close of the operation the contents of the tank will stand twelve feet deep or over. In other words, the dilution of the liquor must be in such proportion that at the close of the operation the liquid will stand in a tank of the given dimensions to about the depth of twelve feet when four thousand five hundred pounds of copperas has been taken.
In the case where it is important that the liquor be kept practically at the point of neutrality during the operation this may be done by continually testing the liquor-as, for instance, with Congo-red solution. As the operation proceeds a yellow precipitate is formed having the definite composition of that is, a hydrated basic ferric oxid. Care has to be exercised that no soda or equivalent be added beyond the pointof neutrality, as this would precipitate ferrous hydrate, which would be oxidized to ferric hydrate, thuscontaminating the compound.
' As an intermediate stepin the process it will be seen that the ferrous liquor upon being blown throws down the basic ferric sulfate, and it is the function of the compara-.
tively large mass of water used to hydrolize this sulfate into the basic ferric hydrateabove described, or if the water he previously added, so that the blowing takes place in the presence of sufficient water to hydrolize the basic ferric sulfate, this salt will be hydrolized as formed with formation of basic ferric hydrate. It is well understood that water in suflicient quantities exerts a strong decomposing influence on all such salts as are composed of a weak base combined with a strong acid or of a strong base with a Weak acid, and such reactions'are designated by the term hydrolysis. (Introduction to Physical Chemistry: \Valker, London, 1899, pages 278-282.)
Basic ferric sulfate formed by blowing the ferrous liquor is an example of the first class above mentioned and is therefore on the addition of sufficient water resolved into sulfuric acid and basic ferric hydrate. The acid is neutralized and set free by the gradual addition of sodium or other carbonate, thereby preventing the reaction from reaching an equilibrium and determining the complete decomposition of the basic ferric sulfate. It will thus be seen that the added water is the active precipitating agent and that the reaction is effected by hydrolysis.
To complete the process, the liquor after being treated in the tank bis run into the tank 0, from which it is forced by air -pressure through the pipe 0' into the filter d. The sulfate or chlorid solution runs 01?, and the hydrated basic ferric oxid which remains as a filtrate is collected and washed and dried at a low heat. The hydrated basic ferric oxid can be dried in its original state or calcined to produce the various shades of iron-oxid reds. The calcination will require little furnacing, producing shadestsurpassing. those produced by the calcination of copperas and giving also an oxid which requires no levigation or grinding, being in a very fine state of subdivision and having no trace of acid or undecomposed sulfate.
If instead of carbonate of soda carbonate of magnesia be added to a ferrous-sulfate liquor, the resulting liquor would contain sulfate of magnesia, which could be crystallized and used as Epsom salts. If carbonate of calcium or carbonate of barium be used with ferrous-sulfate liquor, the same bright-yellow precipitate is obtained, but it contains all the calcium or barium as the sulfate of those metals'. The product obtained by either of these methods would be about three times the quantity of the precipitate formed by treating the ferrous-sulfate liquor with carbonate of soda. A sample of this basic ferric hydrate when mixed as a paint was found to possess an absorption of oil three times as much as Rochelle, two and one-half times as great as standard French ocher, seven and one-half times that of white lead, and three times that of pure zinc oxid. It also had four times the covering power of white lead, twice the covering power of zinc-white, and from two to three times the covering power of the finest French ocher.
My process is equally adapted to the treatment of either a ferrous-sulfate or a ferrouschlorid liquor. In both cases when an alkaline carbonate is used in carrying out my process the basic ferric oxid is obtained purer, as the snlfatesand chlorids of alkalies remain in solution. If ferrous-chlorid liquor be treated with an alkaline-earth carbonate-such as barium, calcium, or strontium-then chlorids of these metals are obtained in solution and the pure basic ferric oxid is precipitated. The resulting liquor can be evaporated and utilized in the usual way or may be used for making blanc fixe in case a carbonate of barium has been employed or pearl-hardening if calcium-carbonate has been employed. When ferrous-sulfate liquor is treated with an alkaline-earth carbonate, the basic ferric basic ferric hydrate.
2. The process of preparing basic ferric hydrate from ferrous-sulfate liquors, which consists in blowing with aira mass in a substantially neutralized condition and precipitating basic ferric sulfate in the presence of a sufficient volume of water to hydrolize the basic sulfate into the basic ferric hydrate. A
3. The process of preparing basic ferric hydrate from ferrous sulfate or chlorid liquors, which consists in blowing with air a mass in a substantially neutralized condition by a gradual addition of an alkali carbonate or an alkaline-earth carbonate, thus precipitating basic ferric sulfate or chlorid in the presence of a sufl'icient volume of water to hydrolize the basic ferric sulfate or chlorid into the basic ferric hydrate.
4. The process of preparing basic ferric hydrate from ferrous-sulfate liquors, which consists in blowing with air a mass in a substantially neutralized condition by a gradual addition of soda-ash, thus precipitating basic ferric sulfate in the presence of a sufiicient volume of water to hydrolize the basic ferric sulfate into the basic ferric hydrate.
5. The process of preparing basic ferric hydrate from ferrous-sulfate liquors, which consists in blowing with air in the substantially neutralized condition described, by a gradual addition of soda-ash in aqueous solution,thus precipitating basic ferric sulfate in the presence of a sufficient volume of water to hydrolize the basic ferric sulfate into basic ferric 5 hydrate.
the condition described, thus precipitating basic ferric sulfate in the presence of a sufficient volume of water to hydrolize the basic sulfate into the basic ferric hydrate.
8. The process of preparing basic ferric hydrate from ferrous-sulfate liquors, which consists in blowing with air a mass in the condition described, thus precipitating basic ferric sulfate in the presence of a sufficient volume of water to hydrolize the basic sulfate into the basic ferric hydrate, filtering and washing the hydrate.
9. The process of preparing basic ferric hydrate from ferrous sulfate or chlorid liquors, which consists in blowing with air a mass brought to the condition described, thus precipitating basic ferric sulfate or chlorid in the presence of a suificient volume of water to hydrolize the basic sulfate or chlorid into the basic ferric hydrate,filtering and washing the hydrate and drying the same.
10. As an article of manufacture, the light ferric hydrate, having the formula the same being of a golden-yellow color, suitable for pigment,fine and velvety to the touch, absorbing more oil than standard French ocher, zinc-white or white lead, and also having more covering power than these pigments.
Signed by me at Cleveland, Ohio, this 19th day of July, 1900.
ALEXANDER SYDNEY RAMAGE.
Witnesses:
VICTOR O. LYNCH, A. H. PARRATT.
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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2608468A (en) * 1948-05-14 1952-08-26 Kennedy M Nahas Method of producing ferric hydrate from aniline sludge
US2620261A (en) * 1947-04-30 1952-12-02 C K Williams & Co Method of making iron oxide pigment
US2733128A (en) * 1956-01-31 Process for the recovery of u in the
US2904402A (en) * 1955-12-30 1959-09-15 Northern Pigment Company Ltd Method of forming uniform uncontaminated iron oxide for pigment and other uses
US3164463A (en) * 1961-10-10 1965-01-05 Dravo Corp Process for handling iron laden wastes in steel mills
US3867516A (en) * 1971-05-03 1975-02-18 Mines Fond Zinc Vieille Method of preparing a pigment on an iron oxide base

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2733128A (en) * 1956-01-31 Process for the recovery of u in the
US2620261A (en) * 1947-04-30 1952-12-02 C K Williams & Co Method of making iron oxide pigment
US2608468A (en) * 1948-05-14 1952-08-26 Kennedy M Nahas Method of producing ferric hydrate from aniline sludge
US2904402A (en) * 1955-12-30 1959-09-15 Northern Pigment Company Ltd Method of forming uniform uncontaminated iron oxide for pigment and other uses
US3164463A (en) * 1961-10-10 1965-01-05 Dravo Corp Process for handling iron laden wastes in steel mills
US3867516A (en) * 1971-05-03 1975-02-18 Mines Fond Zinc Vieille Method of preparing a pigment on an iron oxide base

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