US82154A - Improved process - Google Patents

Improved process Download PDF

Info

Publication number
US82154A
US82154A US82154DA US82154A US 82154 A US82154 A US 82154A US 82154D A US82154D A US 82154DA US 82154 A US82154 A US 82154A
Authority
US
United States
Prior art keywords
sulphate
improved process
tub
steam
distilled water
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
Publication date
Application granted granted Critical
Publication of US82154A publication Critical patent/US82154A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F11/00Compounds of calcium, strontium, or barium
    • C01F11/46Sulfates

Definitions

  • This process is, a simple and effective series of operations for treating the mineral known as sulphate of baryta,'or heavy spar, so called, whereby the mineral is refined and reduced to a fine powder, known in commerce as sulphate of ba'rytes.
  • the tilt (as the crude, heavy spar, as it comes from the mine, is called,) is placed in a vat, A, ( Figure 1,) and covered-with distilled water, which is made to boil by or with steam, conducted through the pipe a to the bottom of the tifi' in the vat.
  • crushed tifi' is then placed in the tub or tank B, ( Figure-2,) and again'boiled by steam througha pipe, 6, in a weak solution of any suitable acid, as sulphuric acid.
  • This operation extracts iron and other impurities usually found accompanying the tifl'.
  • the acid solution is then drawn oil and replaced by a weak solution of silicate of soda in distilled water, in which the crushed tifi' is again boiled by means of steam as before, the boiling process lasting about an hour.
  • This bath is then drawn oil from the vat, and replaced by a saturated solution of alum-water. and again stirred oragitated as before.
  • the product thus far treated is then conveyed by a chute, c, orother suitable means, to a copper dryingpan or pans, D, ( Figure 4,) in which the mineral is dried by means of steam-pipes or other suitable heatingapparatus.
  • the mineral When dried, the mineral is conveyed to any suitable grindingmill, and reduced to a fine powder.

Description

'W. M. PAGE & E. B. KRAUSSE. PROCESS or PREPARING SULPHATE 0F BARYTES.
Patented Sept. 15
gut uh tat-2s gaunt @fi'inL WILLIAM M. PAGE AND EMlL B. KRAUSSE. OF ST. LOUIS, MISSOURI.
Letters PatentNo. 82,154, dated September 15, 1868.
IMPROVED PROCESS. OF PREPARING SULPHATE 0F BARYTES.
To ALL WHOM IT MAY CONCERN:
Be it known that we, WILLIAM M. Pass and EMIL B. KRAUSSE, of St. Louis, in the county of St. Louis,
and State of Missouri, have invented'a new and improved Process for Preparing Sulphate of Barytes and we do hereby declare that the following is a full, clear, and exact description thereof, 'which will enable those skilled in the art to make and use thesame, reference being had to the accompanying drawings, forming part of this specification.
This process is, a simple and effective series of operations for treating the mineral known as sulphate of baryta,'or heavy spar, so called, whereby the mineral is refined and reduced to a fine powder, known in commerce as sulphate of ba'rytes. r
The accompanying drawings represent the apparatus employed in the difi'erent stages of too process.
The tilt, (as the crude, heavy spar, as it comes from the mine, is called,) is placed in a vat, A, (Figure 1,) and covered-with distilled water, which is made to boil by or with steam, conducted through the pipe a to the bottom of the tifi' in the vat.
After being boiled for about an hour it is taken out and dried, and crushedin any suitablo crushing-mill;
The crushed tifi' is then placed in the tub or tank B, (Figure-2,) and again'boiled by steam througha pipe, 6, in a weak solution of any suitable acid, as sulphuric acid.
This operation extracts iron and other impurities usually found accompanying the tifl'.
The acid solution is then drawn oil and replaced by a weak solution of silicate of soda in distilled water, in which the crushed tifi' is again boiled by means of steam as before, the boiling process lasting about an hour.
The till thus treated, is then discharged into avat, C, (Figure 3,) which in practice is located underthe tub B,- so that the till may be readily discharged therein.
In this vat the till" is washed in distilled water and silicate of soda, by means of any suitable stirringmechanism or hand-implement.
This bath is then drawn oil from the vat, and replaced by a saturated solution of alum-water. and again stirred oragitated as before.
The product thus far treated, is then conveyed by a chute, c, orother suitable means, to a copper dryingpan or pans, D, (Figure 4,) in which the mineral is dried by means of steam-pipes or other suitable heatingapparatus.
When dried, the mineral is conveyed to any suitable grindingmill, and reduced to a fine powder.
From the mill it is conveyed, by a chute, e, to a mixing-tub, E, (Figure 5,) provided with any suitably constructed mixing-mechanism, as that shown, where the mine al is again agitated in distilled water from the tank G, and thus thoroughly mixed for floating. 4
It is then conveyed through a trough, H, about one hundred and, eighty feet in length, to a tank or tub, I, (Figure 6,) and left to settle from the water with which it entered the tub I.
From this tub it is then run out into shallow copper pans and dried.
It is then ready for barrelling as the trade'article of sulphate of barytc s.
These are the general steps of' the operation, but we desire to be understood as not limiting ourselves to the precise means for producing the various operations, or the particular form or sequence of the apparatus, or arrangement of the same, as some changes may be made in the same'without materially ali'ectingthe success of the process.
It will be seen from the foregoing that the principal features of improvement oi our process over that commonly used, are- First, the boiling of the tifl in water or by steam-vapor to render it more friable.
Second, boiling the tiff in acid solution to remove impurities,
Third, the use of silicate of soda to remove such impurities as are not affected by the acid-solutions.
Fourthhthe use of alum-solutions to whiten the tifi'.
Fifth, the use of distilled water to obtain sulphate of berytes in greater purity.
And' as each of these features constitutes in-itself a. new and advantageous feature; not dependent upon the others, we desire to secure them agaii'lst appropriation in ether combinatio'ns.
Having thus described our invention; what we claim as new,' and'desire to secure by Letters Phtht, is
The vprocess, substantially as described, for heating sulphate of .bary'ta, and producing therefrom the refined 3 product known to the trade as sulphate of barytes." v
' WILLIAM M. PAGE,
EMIL B. KRAUSSE. Witnesses:
Girls.- H. Emma, Louis "Rmumm.
US82154D Improved process Expired - Lifetime US82154A (en)

Publications (1)

Publication Number Publication Date
US82154A true US82154A (en) 1868-09-15

Family

ID=2151647

Family Applications (1)

Application Number Title Priority Date Filing Date
US82154D Expired - Lifetime US82154A (en) Improved process

Country Status (1)

Country Link
US (1) US82154A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100198333A1 (en) * 2009-01-31 2010-08-05 Macatangay Edwin E Preform for and an endoluminal prosthesis

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100198333A1 (en) * 2009-01-31 2010-08-05 Macatangay Edwin E Preform for and an endoluminal prosthesis

Similar Documents

Publication Publication Date Title
US82154A (en) Improved process
GB230916A (en) An improved method for the extraction of aluminium materials
US209488A (en) Improvement in manufacture of alum-cake and sulphate of alumina
US1913960A (en) Process of producing a composition for decolorizing and purifying oils
US1936806A (en) Process of making strontium carbonate
US1528218A (en) Process of manufacturing pure cellulose from wood
US1194014A (en) Methob oe beeiming wool-gbease
US1455995A (en) Bleaching earth
US120380A (en) Improvement in methods of utilizing the waste chloride of zinc in treating paper
US353092A (en) Carl steffen
GB333426A (en) Process of and apparatus for effecting continuous digestion in the extraction of cellulose
US289836A (en) hobson
US96241A (en) Improved method of recovering grease from waste soap-liquors
AT131409B (en) Process for the extraction of beryllium compounds from minerals containing beryllium.
US1185262A (en) Process for producing oil and cellulosic material from nuts.
AT110889B (en) Process for digesting clay and other raw materials containing alumina with acids.
US96423A (en) Improvement in rendering animal fats
US772129A (en) Process of making hydroxy stearic acid.
US1354376A (en) Method and process of making lanolin
US251887A (en) Grape-sugar
US153251A (en) Improvement in treating cotton-seed oil for paint
US664437A (en) Treating white lead.
US216483A (en) Improvement in separating potash from ashes
US266452A (en) Half to g
US91654A (en) Improved ltjbricatino-oh