US137072A - Improvement in the manufacture of boracic acid - Google Patents

Improvement in the manufacture of boracic acid Download PDF

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US137072A
US137072A US137072DA US137072A US 137072 A US137072 A US 137072A US 137072D A US137072D A US 137072DA US 137072 A US137072 A US 137072A
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steam
boracic acid
manufacture
improvement
acid
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/08Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
    • C01B35/10Compounds containing boron and oxygen

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  • my invention consists of a new method of separating, by superheated steam, the hydrate of boracic acid from the native borate of lime.
  • a loose grating or false bottom, D serves to support the contents.
  • an opening provided with a well-fitting door, E is left in the side of the cylinder to remove the exhausted mass.
  • the pipe 0 leads into a brick or metal-lined chamber, F, from which another pipe, G, opens into another similar chamber, and thence into the atmosphere.
  • the superheating of the steam may be done in the well-known manner, by conducting steam through an iron apparatus heated from the outside, butI prefer to employ ordinary high-pressure steam, to make it issue in a jet from a nozzle, which jet sucks up and carries along the hot gas produced by the combustion of cokes in a separate fire-place, as the presence of such gas does not interfere with the operation.
  • the temperature of the steam entering the cylinder A ought to be so high that it will leave the cylinder at the top, after having traversed the contents, with a temperature above the boiling-point of water, so that no condensation of steam can take place within the cylinder.
  • the temperature of the chamber F must be not much below the boiling point of water, which is effected by proper dimensions and material.
  • the steam escaping through G carries along still a comparatively small percentage of boraeic acid, and passes, therefore, a second chamber, in which a temperature of about 190 Fahren heit allows a portion of the steam to condense.
  • the steam which leaves this second chamber contains practically no more boracic acid, and
  • the purpose of my invention can also be achieved by using an iron cylinder instead of one made of brick, or by employing horizontal retorts instead of vertical ones.
  • the retorts, horizontal or vertical, may also be heated from the outside and ordinary steam passed through. Thus the superheating of the steam takes place inside the retorts.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Glass Compositions (AREA)
  • Paper (AREA)

Description

F. GUTZKGW.
Manufacture of Bnracic'Acid 10.131072. 1 PatentedMarch25 ,1873.
ii L4 7 ing; and consists of an upright cylinder, A,
0, branches off to remove the products of dis- NITE STATES FREDERICK GUTZKOW, OF SAN FRANCISCO, CALIFORNIA.
- IMPROVEMENT IN THE MANUFACTURE OF BORACIC ACID.
Specification forming part of Letters Patent No. 1 37,072, dated March 25, 1873.
To all whom it may concern.-
Be it known that I, FREDERICK GU'rzKow, of the city and county of San Francisco, State of Oalifornia,have invented an Improved Process of Obtaining Boracic Acid from Borate of Lime and I do hereby declare that the best mode which I have discovered for performing the said process is described in the following specification,together with the best apparatus known to me for that purpose.
The nature of my invention consists of a new method of separating, by superheated steam, the hydrate of boracic acid from the native borate of lime.
Theapparatus which I prefer to use for that purpose is set forth in the accompanying drawmade of common brick, about two feet in diameter and ten feet high. Through the cover which closes it at the top a funnel, B, passes, and serves to introduce the mass to be distilled. Underneath that cover a pipe or flue,
tillation. About one foot above the bottom of the cylinder A a loose grating or false bottom, D, serves to support the contents. On a plane with the grate D an opening provided with a well-fitting door, E, is left in the side of the cylinder to remove the exhausted mass. Below the grate D the superheated steam enters. The pipe 0 leads into a brick or metal-lined chamber, F, from which another pipe, G, opens into another similar chamber, and thence into the atmosphere.
The superheating of the steam may be done in the well-known manner, by conducting steam through an iron apparatus heated from the outside, butI prefer to employ ordinary high-pressure steam, to make it issue in a jet from a nozzle, which jet sucks up and carries along the hot gas produced by the combustion of cokes in a separate fire-place, as the presence of such gas does not interfere with the operation.
The temperature of the steam entering the cylinder A ought to be so high that it will leave the cylinder at the top, after having traversed the contents, with a temperature above the boiling-point of water, so that no condensation of steam can take place within the cylinder.
The manner in which I operate is the following: I place a suitable quantity of powdered borate of lime into a trough, sprinkle over it so much diluted sulphuric acid as, in the following operation, the decomposition of the ho rate will require, and mix the stiff pulp with half the weight of ordinary cokes in order to. facilitate the passage of the steam. Then I bring this mixture through the funnel B into the cylinder A, which is still partially filled with the hot residue of a former operation, close the funnel, and apply steam. The hydrate of boracic acid will immediately commence to escape, with the steam, through the pipe 0, and cover the windings of 'the cham ber F in fine large crystals. The temperature of the chamber F must be not much below the boiling point of water, which is effected by proper dimensions and material. The steam escaping through G carries along still a comparatively small percentage of boraeic acid, and passes, therefore, a second chamber, in which a temperature of about 190 Fahren heit allows a portion of the steam to condense. The steam which leaves this second chamber contains practically no more boracic acid, and
may escape into the atmosphere, together with the sulphurous gas formed by the action of the cokes on any excess of sulphuric acid employed.
In the first chamber F only the dry hydrate of boracic acid will settle and form at once an article of commerce 5 in the second chamber, a weak solution of boracic acid in water, which,
While still hot, is mixed with a little caustic lime. After cooling, the borate of lime, which is nearly insoluble in cold water, will separate.
It is added to the'native borate of lime and worked over. From time to time-say, every two hours-the steam is shut off, the door E unscrewed, the lowermost portion of the contents withdrawn, while bars, not shown in the figure, temporarily support the bulk. Then... the door is secured, a fresh portion of the borate of lim e is let in through the funnel, steam turned on, and the operation resumed.
The mass withdrawn is entirely exhausted, and I consider it my discovery that boracic acid can be completely expelled by steam alone in the manner described. The residue consists principally of sulphate of lime and cokes. It is thrown into a trough provided, as false bottom, with a large-holed sieve." Water is added, which is rapidly absorbed by the gypsum. More water converts it into'a thin pulp, which the sieve only the cokes remain. They are,
, without any further manipulation, used over agam.
Though I prefer the apparatus described above for the distillation process, because it allows a continuous working, submits the most exhausted mass to the hottest steam and the richest to the coldest, the purpose of my invention can also be achieved by using an iron cylinder instead of one made of brick, or by employing horizontal retorts instead of vertical ones. The retorts, horizontal or vertical, may also be heated from the outside and ordinary steam passed through. Thus the superheating of the steam takes place inside the retorts.
Having thus described my invention, I do not claim the process as described in the En glish patent of Bell'and Schofield in 1854.- neither do I claimas my invention the English patent issued to one Beatson in 1855, as their processes will not answer to accomplish the object designed to be effected by the use of my process; but
What I do claim, and desire to secure by Letters Patent, is-
The separation of boracic acid from borate of lime by distillation with superheated steam, substantially as set forth and described.
In witness whereof I have hereunto set my hand and seal.
FREDERICK GUTZKOW. [L. s.]
Witnesses:
(J. W. M. SMITH, PHILIP MAHLEB.
US137072D Improvement in the manufacture of boracic acid Expired - Lifetime US137072A (en)

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2898192A (en) * 1957-05-01 1959-08-04 Horizons Inc Production of boric acid
US3026178A (en) * 1958-10-16 1962-03-20 Callery Chemical Co Preparation of boric oxide and boric acid
US3454359A (en) * 1966-04-29 1969-07-08 Stauffer Chemical Co Process for producing boric acid from alkali metal borates
US3650690A (en) * 1968-10-18 1972-03-21 Stauffer Chemical Co Boric acid production
WO2007048440A1 (en) * 2005-10-25 2007-05-03 Fci Electrique France Clamping device for tightening and clamping a strip and clamping assembly comprising such a clamping device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2898192A (en) * 1957-05-01 1959-08-04 Horizons Inc Production of boric acid
US3026178A (en) * 1958-10-16 1962-03-20 Callery Chemical Co Preparation of boric oxide and boric acid
US3454359A (en) * 1966-04-29 1969-07-08 Stauffer Chemical Co Process for producing boric acid from alkali metal borates
US3650690A (en) * 1968-10-18 1972-03-21 Stauffer Chemical Co Boric acid production
WO2007048440A1 (en) * 2005-10-25 2007-05-03 Fci Electrique France Clamping device for tightening and clamping a strip and clamping assembly comprising such a clamping device

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