US572512A - Phosphates of alkalies - Google Patents
Phosphates of alkalies Download PDFInfo
- Publication number
- US572512A US572512A US572512DA US572512A US 572512 A US572512 A US 572512A US 572512D A US572512D A US 572512DA US 572512 A US572512 A US 572512A
- Authority
- US
- United States
- Prior art keywords
- alkalies
- phosphates
- phosphoric acid
- salts
- phosphate
- 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
- 239000003513 alkali Substances 0.000 title description 38
- 235000021317 phosphate Nutrition 0.000 title description 28
- 150000003013 phosphoric acid derivatives Chemical class 0.000 title description 18
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 48
- 150000003839 salts Chemical class 0.000 description 26
- 239000011780 sodium chloride Substances 0.000 description 26
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 24
- 238000000034 method Methods 0.000 description 24
- 238000004519 manufacturing process Methods 0.000 description 16
- NBIIXXVUZAFLBC-UHFFFAOYSA-K [O-]P([O-])([O-])=O Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 14
- 239000010452 phosphate Substances 0.000 description 14
- 239000000243 solution Substances 0.000 description 14
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 12
- 239000003518 caustics Substances 0.000 description 10
- LWIHDJKSTIGBAC-UHFFFAOYSA-K Tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 8
- 239000004135 Bone phosphate Substances 0.000 description 6
- BVKZGUZCCUSVTD-UHFFFAOYSA-N Carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 6
- WGSLWEXCQQBACX-UHFFFAOYSA-N Chlorin Chemical compound C=1C(C=C2)=NC2=CC(C=C2)=NC2=CC(C=C2)=NC2=CC2=NC=1CC2 WGSLWEXCQQBACX-UHFFFAOYSA-N 0.000 description 6
- 239000002253 acid Substances 0.000 description 6
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium monoxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 6
- 230000000875 corresponding Effects 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N Calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 description 4
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- VWDWKYIASSYTQR-UHFFFAOYSA-N Sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 4
- 235000015450 Tilia cordata Nutrition 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 150000001340 alkali metals Chemical class 0.000 description 4
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 4
- 239000004568 cement Substances 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 238000005868 electrolysis reaction Methods 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 150000002823 nitrates Chemical class 0.000 description 4
- GRYLNZFGIOXLOG-UHFFFAOYSA-N nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 4
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Inorganic materials [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 description 4
- 235000010333 potassium nitrate Nutrition 0.000 description 4
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 4
- JUNWLZAGQLJVLR-UHFFFAOYSA-J Calcium pyrophosphate Chemical compound [Ca+2].[Ca+2].[O-]P([O-])(=O)OP([O-])([O-])=O JUNWLZAGQLJVLR-UHFFFAOYSA-J 0.000 description 2
- 229910000754 Wrought iron Inorganic materials 0.000 description 2
- 241000209149 Zea Species 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 235000012255 calcium oxide Nutrition 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 229910052570 clay Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 235000005824 corn Nutrition 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- CWYNVVGOOAEACU-UHFFFAOYSA-N fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- ABLZXFCXXLZCGV-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 description 2
- 229940072033 potash Drugs 0.000 description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 2
- 235000015320 potassium carbonate Nutrition 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000012266 salt solution Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/14—Alkali metal compounds
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
- A61K8/24—Phosphorous; Compounds thereof
Definitions
- n NORRIS PETERS'CO. PHOTD-LITNO., wnumomu n c UNITED STATES PATENT OFFICE.
- the phosphates obtained electrolytically in this manner may also beapplied directly to the manufacture of caustic alkalies, for instance, with caustic lime.
- Salts as chili saltpeter and chlorid of sodium, and so on, which do not undergo double decomposition are, in the presence of phosphoric acid, converted by electrolysis into products which can be directly split up, whereby the phosphoric acid returns to the manufacturing process or may be otherwise employed. It must be re membered that in this process the cost of the splitting-u p operation performed on the salts is completely covered by the recovery of the phosphoric acid and that the yield of caustic alkali is theoretically proportional to the amount of the salt used, as, for instance, nitrate of soda.
- My process possesses the following advantages: First, the process is a continuous one; second, in place of the expensive carbonates of alkalies hitherto used, as, for instance, soda, such cheap salts as chili saltpeter, &c., are employed; third, valuable substances like nitric acid, sulfuric acid, &c., are obtained as by-products; fourth, the concentration of the solution by evaporation may be completely omitted fifth, the alkaline phosphate thus cheaply produced may be directly converted into caustic alkali by treatment, as, for instance, with quicklime, while the phosphoric acid in the shape of phosphate of lime returns to the manufacture or is otherwise employed.
- a is a wrought-iron vessel which is coated with cement or similar material b.
- This vessel is divided by a diaphragm (Z of porous clay or similar substance covered by a coating 0 of cement or similar material.
- That I claim is 1.
- the herein-described process of manufacturing phosphates of the alkalies which consists in forming a bath of phosphoric acid and a bath of one or more of the soluble salts of the alkali metals, associating the said two baths together in an electrical circuit, the said baths being separated by a porous diaphragm and thereupon electrolyzing the said combined baths by passing a currentof electricity therethrough, whereby a mono, di or tri basic phosphate of the alkali employed is produced at the cathode.
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- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Inorganic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Public Health (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Animal Behavior & Ethology (AREA)
- General Health & Medical Sciences (AREA)
- Birds (AREA)
- Veterinary Medicine (AREA)
- Engineering & Computer Science (AREA)
- Epidemiology (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
Description
(RolodeL) H. ALBERT.
PROCESS OF MANUFACTURING PHOSPHATES 0P ALKALIES. No. 572,512. Patented Dec 8, 1896.
l l I I I l l I ,l
n: NORRIS PETERS'CO. PHOTD-LITNO., wnumomu n c UNITED STATES PATENT OFFICE.
HEINRICH ALBERT, OF BIEBRICH, GERMANY, ASSIGN OR TO THE CHEMISOHE WERKE, VORMALS H. (in E. ALBERT, OF SAME PLACE.
[PROCESS OF MANUFACTURING PHOSPHATES OF ALKALIES.
SPECIFICATION forming part of Letters Patent No. 572,dated December 8, 1896.
Application filed January 28, 1896. Serial No. 577,149. (No specimens.)
- To all whom it may ooh/corn;-
Be it known that I, HEINRICH ALBERT, of Biebi'ich-on-the-Rhine, Germany, have invented an Improved Process for the Manufacture of Phosphates of Alkalies, of which the following is a specification.
. double decomposition in the presence of phosphoric acid. The phosphates of alkalies hereby formed by electrolysis are decomposed, forming caustic alkalies, while phosphoric acid, recombined as salt of lime, &c., is recovered.
The process hitherto used for the manufacture of phosphates of the alkalies was never a satisfactory one for the reason that the phosphoric acid obtained from crude phosphate and sulfuric acid was neutralized with alkaline carbonates, whereby the carbonic acid was lost. Even the later methods for producing the corresponding salts directly from the crude phosphate did not yield a profit on account of theunsatisfactory results. I have succeeded in producing the phosphates of the alkalies in a pure state in an economical manner by the action of the electrical current on phosphoric acid and the corresponding salts of the alkalies, such as the nitrates, sulfates, and chlorids, &c., of the alkalies. The reactions occurring, in case nitrate of soda is used, are explained by the following equations:
If solutions ofphosphoric acid and of the salts of the alkalies, like nitrates, sulfates,
and chlorids, &c., of whatsoever concentratrical current, either at ordinary or an elevated temperature, separation of the respective acids takes place, and nitric acid, sulfuric acid, or chlorin is set free at the anode. In order to obtain the volatile substances like nitric'acid, chlorin, &c., it is only necessary to heat the solutions. Inasmuch as hereby, as Well as by theeifect of the electrolytic process, the volume of the solution in contact with the anode is quickly reduced, a continual addition of fresh salt solution is needed. On the cathode the corresponding phosphate salt is formed, as, for instance, the mono, di, or tri basic phosphate of potash, soda, '&c. The formation of these respective salts de pends on the quantity of salts used on the anode. The process may be interrupted at the proper time for the purpose of obtaining either the mono or the di or tri basic salt. If the solution of phosphoric acid is sufficiently strong, the salts formed are deposited in solid state on the cathode and may be dipped out; otherwise the cathode solution has to be concentrated.
The phosphates obtained electrolytically in this manner may also beapplied directly to the manufacture of caustic alkalies, for instance, with caustic lime. Salts, as Chili saltpeter and chlorid of sodium, and so on, which do not undergo double decomposition are, in the presence of phosphoric acid, converted by electrolysis into products which can be directly split up, whereby the phosphoric acid returns to the manufacturing process or may be otherwise employed. It must be re membered that in this process the cost of the splitting-u p operation performed on the salts is completely covered by the recovery of the phosphoric acid and that the yield of caustic alkali is theoretically proportional to the amount of the salt used, as, for instance, nitrate of soda.
My process possesses the following advantages: First, the process is a continuous one; second, in place of the expensive carbonates of alkalies hitherto used, as, for instance, soda, such cheap salts as Chili saltpeter, &c., are employed; third, valuable substances like nitric acid, sulfuric acid, &c., are obtained as by-products; fourth, the concentration of the solution by evaporation may be completely omitted fifth, the alkaline phosphate thus cheaply produced may be directly converted into caustic alkali by treatment, as, for instance, with quicklime, while the phosphoric acid in the shape of phosphate of lime returns to the manufacture or is otherwise employed.
An apparatus for carrying out my process is shown in the accompanying drawing.
In the drawing, a is a wrought-iron vessel which is coated with cement or similar material b. This vessel is divided by a diaphragm (Z of porous clay or similar substance covered by a coating 0 of cement or similar material.
The phosphorous solution (phosphoric acid) chlorin which is liberated by the process of decomposition escapes through the pipe g. A cock his provided for draining off the liquid when desired.
That I claim is 1. The herein-described process of manufacturing phosphates of the alkalies which consists in forming a bath of phosphoric acid and a bath of one or more of the soluble salts of the alkali metals, associating the said two baths together in an electrical circuit, the said baths being separated by a porous diaphragm and thereupon electrolyzing the said combined baths by passing a currentof electricity therethrough, whereby a mono, di or tri basic phosphate of the alkali employed is produced at the cathode.
2. The herein-described process for the manufacture of caustic alkalies which consists in forming a bath of phosphoric acid and a bath of one or more of the soluble salts of the alkali metals, associating the said two baths together in an electrical circuit, the said baths being separated by a porous diaphragm and thereupon electrolyzing the said combined baths by passing a current of electricity therethrough, whereby a mono, di or tri basic phosphate of the alkali employed is produced at the cathode, and treating the phosphate of the alkali produced with lime, substantially as described.
HEINRICH ALBERT.
\Vitnesses:
J EAN GRUND, FRANK H. MAsoN.
Publications (1)
Publication Number | Publication Date |
---|---|
US572512A true US572512A (en) | 1896-12-08 |
Family
ID=2641210
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US572512D Expired - Lifetime US572512A (en) | Phosphates of alkalies |
Country Status (1)
Country | Link |
---|---|
US (1) | US572512A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2713554A (en) * | 1949-01-06 | 1955-07-19 | Edgar C Pitzer | Electrolytic method of recovering thorium from monazite sand |
US3269926A (en) * | 1961-10-18 | 1966-08-30 | Knapsack Ag | Process for the electrolytic production of alkali metal phosphates |
-
0
- US US572512D patent/US572512A/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2713554A (en) * | 1949-01-06 | 1955-07-19 | Edgar C Pitzer | Electrolytic method of recovering thorium from monazite sand |
US3269926A (en) * | 1961-10-18 | 1966-08-30 | Knapsack Ag | Process for the electrolytic production of alkali metal phosphates |
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