US747291A - Process of extracting potassium chlorid from fuci and algæ. - Google Patents

Process of extracting potassium chlorid from fuci and algæ. Download PDF

Info

Publication number
US747291A
US747291A US9980102A US1902099801A US747291A US 747291 A US747291 A US 747291A US 9980102 A US9980102 A US 9980102A US 1902099801 A US1902099801 A US 1902099801A US 747291 A US747291 A US 747291A
Authority
US
United States
Prior art keywords
fuci
seaweed
algæ
potassium
potassium chlorid
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
US9980102A
Inventor
David M Balch
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.)
ANSON P STEPHENS
Original Assignee
ANSON P STEPHENS
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 ANSON P STEPHENS filed Critical ANSON P STEPHENS
Priority to US9980102A priority Critical patent/US747291A/en
Application granted granted Critical
Publication of US747291A publication Critical patent/US747291A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21CPRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
    • D21C11/00Regeneration of pulp liquors or effluent waste waters
    • D21C11/12Combustion of pulp liquors

Definitions

  • My improved process relates to the extracro tion of potassium compounds from fuci and algae, and refers more particularly to those classes of seaweeds generally to be found on the American coast, which seaweeds are very rich in alkaline salts and contain scarcely a r 5 trace of iodin, in contradistinction to those families of seaweeds known as Lamzmam'a digitata and Stenophylla found in European waters, which are exceedingly rich in iodin and relatively poor in alkaline salts.
  • the weed is gathered and thoroughly sun-dried, after which it is coarsely cut or broken up. I then dust or coat the material with an alkaline substance, which may consist of an intimate mixture of the carbonate and hydrate of an alkaline earth-such as 0 calcium, barium, strontium, or air-slaked lime, preferably the latter. A mixture of forty grams of lime to each kilogram of the dried seaweed will yield the best results; but the proportions may vary.
  • an alkaline substance which may consist of an intimate mixture of the carbonate and hydrate of an alkaline earth-such as 0 calcium, barium, strontium, or air-slaked lime, preferably the latter.
  • the broken seaweed thus treated is now placed in air-tight retorts, chambers, or in any suitable receptacle and lightly compressed, and heat is applied thereto in any desirable manner within or without the re- 40 ceptacles, the degree of heat being sufficiently high to completely decompose the organic portion of the seaweed, but not high enough to break up the sulfates present, which would result in vitiating the products ulti- 5 mately to be obtained by the sulfids or sulfur lower oxids which would thus be liberated.
  • the effect of the heat upon the commingled seaweed and alkaline substance is to char the material.
  • the retorts or chambers are connected with suitable condensing appliances and to receivers, and all condensible volatile products arising from this modified form of dry distillation, together with the unco'ndensible gases generated, are collected apart. The heating of the retorts or chambers is maintained until no further volatile products are evolved.
  • the non-volatile residuum of the above operation remaining in the retorts comprises a char, which consists of a light porous carbon intimately com mingled with the mineral salts of the fuci and with the added alkaline substance, such as lime.
  • This residuum I may grind or pulverize to a coarse powder, or I may utilize it just as it comes from the retorts. In either case this residuum is lixiviated with the least possible quantity of water, either hot or cold, in suitable vessels, such as percolators or tanks.
  • such solution may be treated by any of the wellknown methods for the purpose of obtaining other potassium compoundssuch, for instance, as saltpeter.
  • the uncondensible gases which are evolved during the charring process and which are collected apart from the volatile condensible products when purified may be used for heat- :00 ing or illuminating purposes.
  • exhausted material remaining in the tanks or percolators after the leaching process may be utilized as fuel, as a basis for fertilizers, or in any other suitable manner.
  • the potassium salts contained in the solution obtained from the char can be technically easily separated from the sodium salts likewise contained therein.

Description

UNITED STATES Patented December 15, 1903.
PATENT OFFICE.
DAVID M. BALCH, OF CORONADO, CALIFORNIA, ASSIGNOR OF ONE-HALF TO ANSON P. STEPHENS, OF CORONADO, CALIFORNIA.
PROCESS OF EXTRACTING POTASSIUM CHLORED FROM FUCl AND ALG/E.
SPECIFICATION forming part of Letters Patent No. 747,291, dated December 15, 19031. Application filed March 24;, 1902. Serial No. 99,801. (No specimens.)
To a whom it may concern:
Be it known that I, DAVID M. BALCH, a citizen of the United States of America, residing at Coronado, in the county of San Diego and State of California, have invented a new and useful Process of Extracting Potassium Chlorid from Fuci and Algte, of which the following is a specification.
My improved process relates to the extracro tion of potassium compounds from fuci and algae, and refers more particularly to those classes of seaweeds generally to be found on the American coast, which seaweeds are very rich in alkaline salts and contain scarcely a r 5 trace of iodin, in contradistinction to those families of seaweeds known as Lamzmam'a digitata and Stenophylla found in European waters, which are exceedingly rich in iodin and relatively poor in alkaline salts.
The object attained by my process is the economical manufacture of potassium compounds in merchantable quantities, to accomplish which I proceed as follows:
First. The weed is gathered and thoroughly sun-dried, after which it is coarsely cut or broken up. I then dust or coat the material with an alkaline substance, which may consist of an intimate mixture of the carbonate and hydrate of an alkaline earth-such as 0 calcium, barium, strontium, or air-slaked lime, preferably the latter. A mixture of forty grams of lime to each kilogram of the dried seaweed will yield the best results; but the proportions may vary.
Second. The broken seaweed thus treated is now placed in air-tight retorts, chambers, or in any suitable receptacle and lightly compressed, and heat is applied thereto in any desirable manner within or without the re- 40 ceptacles, the degree of heat being sufficiently high to completely decompose the organic portion of the seaweed, but not high enough to break up the sulfates present, which would result in vitiating the products ulti- 5 mately to be obtained by the sulfids or sulfur lower oxids which would thus be liberated. The effect of the heat upon the commingled seaweed and alkaline substance is to char the material.
Third. The retorts or chambers are connected with suitable condensing appliances and to receivers, and all condensible volatile products arising from this modified form of dry distillation, together with the unco'ndensible gases generated, are collected apart. The heating of the retorts or chambers is maintained until no further volatile products are evolved.
Fourth. The non-volatile residuum of the above operation remaining in the retorts comprises a char, which consists of a light porous carbon intimately com mingled with the mineral salts of the fuci and with the added alkaline substance, such as lime. This residuum I may grind or pulverize to a coarse powder, or I may utilize it just as it comes from the retorts. In either case this residuum is lixiviated with the least possible quantity of water, either hot or cold, in suitable vessels, such as percolators or tanks. The resulting saline solution is perfectly colorless and may now be evaporated to crystallization or to dryness by either sun or artificial heat, leaving a purely White product, which is merchantable potassium chlorid. Thus it 75, will be seen that by the simple and direct methodhereinabove detailed I obtain without further manipulation the product sought, and this product so obtained needs no further purification, the char yielding commer- 8o cially-pure potassium compounds upon lixiviation.
Fifth. Instead of evaporating the saline liquor received from the percolators, such solution may be treated by any of the wellknown methods for the purpose of obtaining other potassium compoundssuch, for instance, as saltpeter.
The condensible volatile products which are released during the charring of the material differ essentially from the vapors yielded by wood under similar treatment, for the reason that the seaweed contains very little cellulose. When these products are more thoroughly examined, they will, no doubt, 5 yield important merchantable material.
The uncondensible gases which are evolved during the charring process and which are collected apart from the volatile condensible products when purified may be used for heat- :00 ing or illuminating purposes.
The exhausted material remaining in the tanks or percolators after the leaching process may be utilized as fuel, as a basis for fertilizers, or in any other suitable manner.
From the foregoing it will be seen that my invention to a great extent depends for the accomplishment of the result upon the presence of the alkaline substances, such as airslaked lime, with which the dried broken seaweed is coated before being treated in the retorts. The action of these alkaline substances seems to favor the complete separation of the soluble from the insoluble mineral salts of the particular fuci under treatment and is of decided advantage in breaking'up and converting into ammonia certain difficultly-decomposable nitrogenous constituents of the seaweed. The efliciency of these alkaline substances, and particularly of air-slaked lime, has been established to my satisfaction by numerous experimental and practical operations, and by the use of these substances I am enabled to extract from the seaweed directly the products sought economically and in merchantable quantities and condition. The decomposition elements which would otherwise contaminate the product obtained are either prevented or removed by the presence of the finely-divided lime or other alkaline substance in the retorts or other heatingreceptacle.
The potassium salts contained in the solution obtained from the char can be technically easily separated from the sodium salts likewise contained therein.
It is obvious that changes might be made in the foregoing process and in the ingredients used, the manner of compounding, and the proportions. Hence I do not wish to limit myself to the exact method herein set forth; but
What I claim as new, and desire to secure by Letters Patent, is
1. The herein-described process of treating seaweed for the extraction of potassium salts therefrom consisting in drying the seaweed, coarsely cutting or breaking it up, dusting the weed with lime or other alkaline subtance, placing the seaweed in air-tight receptacles under pressure, heating the receptacles to decompose the organic portion of the weed and charring the material, grinding or pulverizing the charred residuum, lixiviating the residuum, and evaporating the clear solution obtained thereby directly yielding colorless merchantable potassium chlorid.
2. The herein-described process of treating seaweed for the extraction of potassium salts therefrom consisting in drying the seaweed, coarsely cutting or breaking it up, dusting the weed with lime or other alkaline substance, placing the seaweed in air-tight receptacles,heating the receptacles to decompose the organic portion of the weed and charring the material, grinding or pulverizing the charred residuum, lixiviating the residuum, and evaporating the clear solution obtained thereby directly yielding colorless merchant able potassium chlorid.
. In witness that I claim the foregoing I have hereunto subscribed my name this 15th day of March, 1902.
DAVID M. BALOH.
Witnesses:
HENRY T. HAZARD, G. E. HARPHAM.
US9980102A 1902-03-24 1902-03-24 Process of extracting potassium chlorid from fuci and algæ. Expired - Lifetime US747291A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US9980102A US747291A (en) 1902-03-24 1902-03-24 Process of extracting potassium chlorid from fuci and algæ.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US9980102A US747291A (en) 1902-03-24 1902-03-24 Process of extracting potassium chlorid from fuci and algæ.

Publications (1)

Publication Number Publication Date
US747291A true US747291A (en) 1903-12-15

Family

ID=2815785

Family Applications (1)

Application Number Title Priority Date Filing Date
US9980102A Expired - Lifetime US747291A (en) 1902-03-24 1902-03-24 Process of extracting potassium chlorid from fuci and algæ.

Country Status (1)

Country Link
US (1) US747291A (en)

Similar Documents

Publication Publication Date Title
US747291A (en) Process of extracting potassium chlorid from fuci and algæ.
US1631252A (en) Product obtained from molasses and process of preparing same
US1542006A (en) Decolorizing carbon particularly for medicinal use
GB258035A (en) Improved treatment of the black liquor obtained in the manufacture of wood fibre by the soda process
US1472320A (en) Process for preparing a fodder from straw or other materials characterized by their contents of raw fiber
US3374222A (en) Separating levoglucosan and carbohydrate derived acids from aqueous mixtures containing the same by treatment with metal compounds
US2641542A (en) Detoxifying tung meal
US3309355A (en) Levoglucosan production by pyrolysis of cellulosic material
US1298477A (en) Process of treating waste sulfite liquors, &c.
US1298479A (en) Process for the treatment of waste liquors from soda pulp processes, &c.
US714502A (en) Process of extracting zinc from zinc-skimmings.
US1925204A (en) Art of producing activated charcoal from nitrogenous material
US1315889A (en) Per westin
US1358162A (en) Process for producing a highly-active decolorizing-charcoal
US356292A (en) Extracting bromine and iodine from bittern
US1941760A (en) Method of producing valuable prod
US1543763A (en) Decolorizing carbon and process of producing the same
US489010A (en) Process of making fertilizer from tank-water
US1731677A (en) Insecticide and process of making the same
US1530536A (en) Process for the manufacture of decolorizing charcoal of high activity
US714503A (en) Process of extracting zinc from zinc-skimmings.
US119224A (en) Improvement in the manufacture of paper-pulp
US794481A (en) Process of manufacturing fuel from seaweeds.
US1772216A (en) Method of treating and utilizing the black liquor obtained in the sodapulp process
US245661A (en) Theodoe richters