US5384A - Improvement in decomposing potash-feldspar for obtaining certain salts - Google Patents
Improvement in decomposing potash-feldspar for obtaining certain salts Download PDFInfo
- Publication number
- US5384A US5384A US5384DA US5384A US 5384 A US5384 A US 5384A US 5384D A US5384D A US 5384DA US 5384 A US5384 A US 5384A
- Authority
- US
- United States
- Prior art keywords
- potash
- feldspar
- sulphate
- lime
- improvement
- 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
Links
- 239000010433 feldspar Substances 0.000 title description 24
- 239000011780 sodium chloride Substances 0.000 title description 10
- 150000003839 salts Chemical class 0.000 title description 8
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 40
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 36
- 235000015450 Tilia cordata Nutrition 0.000 description 36
- 235000011941 Tilia x europaea Nutrition 0.000 description 36
- 239000004571 lime Substances 0.000 description 36
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 24
- 229940072033 potash Drugs 0.000 description 16
- 235000015320 potassium carbonate Nutrition 0.000 description 16
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 16
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 16
- 229910052742 iron Inorganic materials 0.000 description 12
- 239000000203 mixture Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 8
- 235000002639 sodium chloride Nutrition 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- QVQLCTNNEUAWMS-UHFFFAOYSA-N Barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate dianion Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 6
- 206010015150 Erythema Diseases 0.000 description 6
- IATRAKWUXMZMIY-UHFFFAOYSA-N Strontium oxide Chemical compound [O-2].[Sr+2] IATRAKWUXMZMIY-UHFFFAOYSA-N 0.000 description 6
- 229910001864 baryta Inorganic materials 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 6
- 238000005755 formation reaction Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 6
- 235000011164 potassium chloride Nutrition 0.000 description 6
- 239000001103 potassium chloride Substances 0.000 description 6
- 238000000605 extraction Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- LSNNMFCWUKXFEE-UHFFFAOYSA-N sulfonic acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 4
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 4
- 230000004520 agglutination Effects 0.000 description 2
- 230000024126 agglutination involved in conjugation with cellular fusion Effects 0.000 description 2
- 239000011449 brick Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 230000004927 fusion Effects 0.000 description 2
- 230000001590 oxidative Effects 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N silicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/04—Chlorides
- C01D3/08—Preparation by working up natural or industrial salt mixtures or siliceous minerals
Definitions
- My invention consists in a method of decomposingfeldspars containing potash by heating them with a sulphate or muriate of another base, by which means are produced a sulphate or muriate of potash and a silicate of the other base employed.
- the feldspars best for the purpose are those containing the largest quantity of potash, and the proportions of materials directed to be used in the processes hereinafter described are calculated for a feldspar containing sixteen per cent. of potash.
- I- decompose feldspar for the production of sulphate of potash by heating together at or above redness a potash-feldspar, lime, or its carbonate, and the sulphate of either lime, baryta, or strontia, and afterward lixiviating the mixture with water.
- I have the materials ground to fine powder and mix them intimately in the proportion of two parts, by weight, of feldspar, one part of lime, or an equivalent quantity of carbonate of lime, and one part of sulphate of lime, which I prefer to the other sulphates.
- the lime maybe dispensed with in the above process if the quantity of sulphate of lime or other sulphate used be increased in the proportion of three parts of sulphate added for one part of lime omitted, and the process conducted as above described; but I prefer the use of lime, as above stated.
- sulphurous-acid gas a cheap and abundant supply of sulphurous-acid gas can be obtained, as from the roasting of sulphurous ores, the use of the sulphate of lime or other sulphate in the mixture may be dispensed with by doubling the quantity of lime or of carbonate of lime before prescribed, and exposing the charge while at a red heat in the furnace to a current of sulphurousacid. gas and air with frequent stirring. Sulphate of lime is thus formed during the process, and the formation of sulphate of potash takes place, as in the former case.
- the mixture is well dried and introduced into a horizontal iron cylinder with an opening only at one end, whichlis closed With an iron door or cover.and luted tight.
- the cylinder is covered on the outside with fire-brick to protect the iron from the action of the fire.
- the cylinder and its contents are to be heated to bright redness for about sixhours.
- the heat should be above the fusing-point of the muriate employed; but I prefer to keep it below the point at which the feldspar would melt, as the charge would then be more difficult to remove from the cylinder.
- the cover is 110w taken oh", and charge raked out as quickly as possible into an iron pot, which is immediately covered and kept closed until the mass is'cool.
- the soluble salts are to be extracted from the mass by 2.
- the method of decomposing potash-feldspar for the production of muriate of potash by heating together a potash-feldspar and the muriate of either soda, lime, or iron at a temperature above the melting-point of ,t-he muriate employed.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Cookers (AREA)
Description
T UNITED STATES PATENT ""FFICE.
R. A. TILGHMAN, OF PHILADELPHIA, PENNSYLVANIA.
Specification forming part of Letters Patent No. 5 ,384, dated December 4, 1847.
ment in Extracting Potash from Feldspars, of
which the following is a full and exact description.
My invention consists in a method of decomposingfeldspars containing potash by heating them with a sulphate or muriate of another base, by which means are produced a sulphate or muriate of potash and a silicate of the other base employed. The feldspars best for the purpose are those containing the largest quantity of potash, and the proportions of materials directed to be used in the processes hereinafter described are calculated for a feldspar containing sixteen per cent. of potash.
I- decompose feldspar for the production of sulphate of potash by heating together at or above redness a potash-feldspar, lime, or its carbonate, and the sulphate of either lime, baryta, or strontia, and afterward lixiviating the mixture with water. I have the materials ground to fine powder and mix them intimately in the proportion of two parts, by weight, of feldspar, one part of lime, or an equivalent quantity of carbonate of lime, and one part of sulphate of lime, which I prefer to the other sulphates. I place the mixture upon thehearth of a reverberatory furnace, and heat it to a bright redness for about eight hours, turning the charge from time to time, so that all parts may receive equal heat. Although the formation of sulphate of potash is most rapid at a high temperature, yet I do not let the heat rise high enough to cause the fusion or agglutination of the mass, as the subsequent extraction of the salt by water is thereby rendered more difficult. The presence of adeoxidizing atmosphere in the furnace being iniurious to the formation of the sulphate of potash, I admit through suitable openings above the level of the fire a sufficient quantity of air into the gases arising from the fuel to preserve the atmosphere in an oxidizing state. When all parts of the charge have remained at a high red heat for from eight to ten hours, I withdraw the charge from the furnace and lixiviate it with hot water repeatedly, as some of the salt adheres obstiuately to the sulphate of lime. The solution of sulphate of potashis then evaporated, the sulphate of lime which deposits during the evaporation being continually removed. When the sulphate of baryta or strontia is used in place of the sulphate of lime the same process is to be pursued; but the extraction of the sulphate of potash by water is more easy, owing to the less solubility of the sulphates of baryta and strontia.
The lime maybe dispensed with in the above process if the quantity of sulphate of lime or other sulphate used be increased in the proportion of three parts of sulphate added for one part of lime omitted, and the process conducted as above described; but I prefer the use of lime, as above stated.
hen a cheap and abundant supply of sulphurous-acid gas can be obtained, as from the roasting of sulphurous ores, the use of the sulphate of lime or other sulphate in the mixture may be dispensed with by doubling the quantity of lime or of carbonate of lime before prescribed, and exposing the charge while at a red heat in the furnace to a current of sulphurousacid. gas and air with frequent stirring. Sulphate of lime is thus formed during the process, and the formation of sulphate of potash takes place, as in the former case.
I decompose feldspar for the production of muriate of potash by heating together a potash-feldspar, and the muriate of either soda, lime, or iron at atemperature above the fusingpoint of the muriate employed. I prefer using muriate of soda or common salt, which I mix with an equal weight of finely-ground feldspar. The mixture is well dried and introduced into a horizontal iron cylinder with an opening only at one end, whichlis closed With an iron door or cover.and luted tight. For the escape of any gas that might tend to burst the cylinder I have a small hole through the upper part of the door,whieh is closed at pleasure by a loosely-fitting plug. The cylinder is covered on the outside with fire-brick to protect the iron from the action of the fire. The
cylinder and its contents are to be heated to bright redness for about sixhours. The heat should be above the fusing-point of the muriate employed; but I prefer to keep it below the point at which the feldspar would melt, as the charge would then be more difficult to remove from the cylinder. The cover is 110w taken oh", and charge raked out as quickly as possible into an iron pot, which is immediately covered and kept closed until the mass is'cool. The soluble salts are to be extracted from the mass by 2. The method of decomposing potash-feldspar for the production of muriate of potash by heating together a potash-feldspar and the muriate of either soda, lime, or iron at a temperature above the melting-point of ,t-he muriate employed.
In testimony whereof I, the said RICHARD ALBERT TILGHMAN, hereto subscribe my name, in the presence of the witnesses whose names are hereto subscribed, on the 13th day of September, A. D. 1847.
RICHARD ALBERT TILGHMAN.
ln presence of- JOSEPH MARQUETTE, WILLIAM EWING.
Publications (1)
Publication Number | Publication Date |
---|---|
US5384A true US5384A (en) | 1847-12-04 |
Family
ID=2065685
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US5384D Expired - Lifetime US5384A (en) | Improvement in decomposing potash-feldspar for obtaining certain salts |
Country Status (1)
Country | Link |
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US (1) | US5384A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020025744A1 (en) * | 1998-05-14 | 2002-02-28 | Mccarthy Peter T. | Methods for creating large scale focused blade deflections |
US6371821B1 (en) | 1996-01-11 | 2002-04-16 | Nature's Wing Fin Designs, Llc | High efficiency hydrofoil and swim fin designs |
US6413133B1 (en) | 1998-05-14 | 2002-07-02 | Mccarthy Peter T. | Methods for creating consistent large scale blade deflections |
US6482059B2 (en) | 1997-05-09 | 2002-11-19 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US6884134B2 (en) | 2002-07-19 | 2005-04-26 | Mccarthy Peter T. | High deflection hydrofoils and swim fins |
US20070213808A1 (en) * | 1997-02-07 | 2007-09-13 | Endosystems Llc | Non-foreshortening intraluminal prosthesis |
-
0
- US US5384D patent/US5384A/en not_active Expired - Lifetime
Cited By (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6719599B2 (en) | 1996-01-11 | 2004-04-13 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US6371821B1 (en) | 1996-01-11 | 2002-04-16 | Nature's Wing Fin Designs, Llc | High efficiency hydrofoil and swim fin designs |
US7101240B2 (en) | 1996-01-11 | 2006-09-05 | Mccarthy Peter T | High efficiency hydrofoil and swim fin designs |
US6497597B2 (en) | 1996-01-11 | 2002-12-24 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US6585548B2 (en) | 1996-01-11 | 2003-07-01 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US6607411B1 (en) | 1996-01-11 | 2003-08-19 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US20070213808A1 (en) * | 1997-02-07 | 2007-09-13 | Endosystems Llc | Non-foreshortening intraluminal prosthesis |
US6482059B2 (en) | 1997-05-09 | 2002-11-19 | Mccarthy Peter T. | High efficiency hydrofoil and swim fin designs |
US6712656B2 (en) | 1998-05-14 | 2004-03-30 | Mccarthy Peter T. | Methods for creating consistent large scale blade deflections |
US6843693B2 (en) | 1998-05-14 | 2005-01-18 | Mccarthy Peter T. | Methods for creating large scale focused blade deflections |
US6918805B2 (en) | 1998-05-14 | 2005-07-19 | Mccarthy Peter T. | Methods for creating consistent large scale blade deflections |
US20020025744A1 (en) * | 1998-05-14 | 2002-02-28 | Mccarthy Peter T. | Methods for creating large scale focused blade deflections |
US6413133B1 (en) | 1998-05-14 | 2002-07-02 | Mccarthy Peter T. | Methods for creating consistent large scale blade deflections |
US6884134B2 (en) | 2002-07-19 | 2005-04-26 | Mccarthy Peter T. | High deflection hydrofoils and swim fins |
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