US502424A - Heinrich precht - Google Patents
Heinrich precht Download PDFInfo
- Publication number
- US502424A US502424A US502424DA US502424A US 502424 A US502424 A US 502424A US 502424D A US502424D A US 502424DA US 502424 A US502424 A US 502424A
- Authority
- US
- United States
- Prior art keywords
- potassium
- phosphate
- soluble
- meta
- precht
- 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
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 18
- 229910019142 PO4 Inorganic materials 0.000 description 14
- 235000021317 phosphate Nutrition 0.000 description 14
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 13
- 239000010452 phosphate Substances 0.000 description 12
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 9
- OQZCJRJRGMMSGK-UHFFFAOYSA-M potassium metaphosphate Chemical compound [K+].[O-]P(=O)=O OQZCJRJRGMMSGK-UHFFFAOYSA-M 0.000 description 9
- 229940099402 potassium metaphosphate Drugs 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 8
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 7
- 238000002844 melting Methods 0.000 description 7
- 230000008018 melting Effects 0.000 description 7
- 239000011591 potassium Substances 0.000 description 7
- 229910052700 potassium Inorganic materials 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 7
- 238000004519 manufacturing process Methods 0.000 description 6
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 6
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 125000005341 metaphosphate group Chemical group 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 239000002253 acid Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- XPPKVPWEQAFLFU-UHFFFAOYSA-J diphosphate(4-) Chemical compound [O-]P([O-])(=O)OP([O-])([O-])=O XPPKVPWEQAFLFU-UHFFFAOYSA-J 0.000 description 3
- 235000011180 diphosphates Nutrition 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Chemical compound [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 3
- 235000011009 potassium phosphates Nutrition 0.000 description 3
- 229940048084 pyrophosphate Drugs 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- XAEFZNCEHLXOMS-UHFFFAOYSA-M potassium benzoate Chemical compound [K+].[O-]C(=O)C1=CC=CC=C1 XAEFZNCEHLXOMS-UHFFFAOYSA-M 0.000 description 2
- RYCLIXPGLDDLTM-UHFFFAOYSA-J tetrapotassium;phosphonato phosphate Chemical compound [K+].[K+].[K+].[K+].[O-]P([O-])(=O)OP([O-])([O-])=O RYCLIXPGLDDLTM-UHFFFAOYSA-J 0.000 description 2
- UEZVMMHDMIWARA-UHFFFAOYSA-N Metaphosphoric acid Chemical compound OP(=O)=O UEZVMMHDMIWARA-UHFFFAOYSA-N 0.000 description 1
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 description 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- 239000012768 molten material Substances 0.000 description 1
- 150000004712 monophosphates Chemical class 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- 229910000027 potassium carbonate Inorganic materials 0.000 description 1
- 235000011181 potassium carbonates Nutrition 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010583 slow cooling Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/38—Condensed phosphates
- C01B25/44—Metaphosphates
- C01B25/445—Metaphosphates of alkali metals
Definitions
- My invention relates to the production of phosphate of potassium and of aluminum.
- the meta phosphate of potassium heretofore produced is insoluble in water or substantially so, and my invention has for its obj ectaprocess whereby phosphates of potassium and of aluminum readily, in fact, completely soluble in water may be readily obtained by conversion of the insoluble into soluble salts, in which all of the contained phosphoric acid is in a form readily soluble in water;
- This I attain as hereinafter more specifically described by subjecting the potassium meta phosphate to a melting process, and if this process is carried out in such manner that the meta phosphate is rapidly cooled, that is to say in such a manner as to prevent crystallization, an amorphous potassium salt of the concentrated metaphosphate that is readily soluble is obtained.
- the potassium meta-phosphate may be obtained in any well-known manner, as for instance by heatingpotassium mono-phosphate (KH,PO,), or by melting, preferably by means of steam, potassium carbonate or potassium chlorid together with metaphosphoric acid in such proportions that the compound will contain one atom of I for each atom of K.
- the melting of the insoluble potassium metaphosphate can be effected with the best advantage in a reverberatory furnace in which the phosphate is heated to such a degree as to render it fluid so that it may be allowed to flow out of a tap-hole. If the melting is effected in a reverberatory furnace provided with an inclined sole or hearth the operation can be made a continuous one by feeding the phosphate into the furnace at the highest and coolest point of the hearth, which should incline toward the source of heat, and allowing the molten material to flow from a tap-hole at the lowest and hottest point of such hearth, and if necessary the material may be raked down the incline so that the salt will be gradually reduced to a fluid state.
- the melting of the phosphate is advantageously eifected by subjecting it to the action of an oxidizing flame as a reducing flame might result in a reduction of the phosphoric acid, which would be detrimental.
- potassium metaphosphate that is completely soluble in water is readily obtained, as above described.
- a basic body such as potash or soda, the quantity of which will correspond to the desired combination or composition, is added to the potassium metaphosphate either before or during the melting of the same.
- the soluble potassium phosphates obtained as above described can be employed in the production of soluble phosphate of alumina or of orthophosphate of potassium soluble in.
- the phosphate of alumina is mixed with the soluble potassium metaphosphate or potassium pyrophosphate or both, obtained as hereinbefore set forth, in any desired proportion within the limit of forty per cent. of phosphate of alumina, the solublepotassium meta or pyro phosphate forming with the phosphate of alumina combinations that are soluble in water and whose solutions do not decompose.
- the phosphate of alumina is added to the potassium meta or pyrophosphate or to a mixture of them, either during the process of melting or to the potassium phosphates in the phosphoric acid solution employed as a starting material, in 1 that a'solution of phosphoric acid contaminated with or rendered impure by alu minais employed in the production of the insoluble phosphates. Should the phosphate of alumina contain a small proportion of iron the latter is also converted into a soluble form.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Compositions Of Oxide Ceramics (AREA)
Description
UNITE STATES PATE T OFFICE HEINRICH PRECHT, or NEU-sTAssFUR GERMANY,
PROCESS OF OBTAINING META OR PYRO PHOSPHORlC -ACID COMBINATIONS.
SPECIFICATION forming part of Letters Patent No. 502,424, dated August 1, 1893. Application filed June 16, 1892. Serial No. 436,945. (No specimens) To all whom it may concern:
Be it known that I, I-IEINRIOHPREOHT, a subject of the King of Prussia, residing at Ne u- Stassfurt, Prussia, Germany, have invented certain new and useful Improvements in and Relating to the Production of Phosphate of Potassium and of Alumina; and I do hereby declare the following to be a full, clear, and exact description of the invention, such as will enable others skilled in the art to which it appertains to make and use the same.
My invention relates to the production of phosphate of potassium and of aluminum.
It is well known that the meta phosphate of potassium heretofore produced is insoluble in water or substantially so, and my invention has for its obj ectaprocess whereby phosphates of potassium and of aluminum readily, in fact, completely soluble in water may be readily obtained by conversion of the insoluble into soluble salts, in which all of the contained phosphoric acid is in a form readily soluble in water; This I attain as hereinafter more specifically described by subjecting the potassium meta phosphate to a melting process, and if this process is carried out in such manner that the meta phosphate is rapidly cooled, that is to say in such a manner as to prevent crystallization, an amorphous potassium salt of the concentrated metaphosphate that is readily soluble is obtained. The potassium meta-phosphate may be obtained in any well-known manner, as for instance by heatingpotassium mono-phosphate (KH,PO,), or by melting, preferably by means of steam, potassium carbonate or potassium chlorid together with metaphosphoric acid in such proportions that the compound will contain one atom of I for each atom of K.
In carrying out my invention I proceed as follows: The insoluble potassium metaphosphate is melted and then allowed to flow into a shallow fiat iron vessel orinto shallow channels for the purpose of rapidly congealing the same so that it will not crystallize but remain in an amorphous condition. A potassium salt of the concentrated metaphosphate is thus formed which by slow cooling would revert into a crystalline and insoluble compound.
The melting of the insoluble potassium metaphosphate can be effected with the best advantage in a reverberatory furnace in which the phosphate is heated to such a degree as to render it fluid so that it may be allowed to flow out of a tap-hole. If the melting is effected in a reverberatory furnace provided with an inclined sole or hearth the operation can be made a continuous one by feeding the phosphate into the furnace at the highest and coolest point of the hearth, which should incline toward the source of heat, and allowing the molten material to flow from a tap-hole at the lowest and hottest point of such hearth, and if necessary the material may be raked down the incline so that the salt will be gradually reduced to a fluid state. The melting of the phosphate is advantageously eifected by subjecting it to the action of an oxidizing flame as a reducing flame might result in a reduction of the phosphoric acid, which would be detrimental.
Practical experience has demonstrated that a potassium phosphate completely soluble in water is obtained when the molten mass contains one molecule of phosphoric acid (P 0 to one molecule of potassium oxid (K 0) or one hundred parts by Weight of anhydrous phosphoric acid, (P 0 or phosphoric acid free from water, to at least 66.2 parts by weight of potassium oxid (K 0). In practice it will, however, be found of advantage to 0perate with a larger proportion of potassium oxid (K 0) so that phosphoric acid in the form of pyrophosphate will in part be present in the molten salt. If the proportion of potassium oxid (K 0) relatively to the phos* phoric acid is such that one partof potassium pyrophosphate to four parts of potassium metaphosphate must be formed in the molten mass, potassium metaphosphate that is completely soluble in water is readily obtained, as above described. In order that these proportions may be obtained a basic body, such as potash or soda, the quantity of which will correspond to the desired combination or composition, is added to the potassium metaphosphate either before or during the melting of the same.
The soluble potassium phosphates obtained as above described can be employed in the production of soluble phosphate of alumina or of orthophosphate of potassium soluble in.
water as follows: In the production of phosphate of alumina soluble in water, the phosphate of alumina is mixed with the soluble potassium metaphosphate or potassium pyrophosphate or both, obtained as hereinbefore set forth, in any desired proportion within the limit of forty per cent. of phosphate of alumina, the solublepotassium meta or pyro phosphate forming with the phosphate of alumina combinations that are soluble in water and whose solutions do not decompose. The phosphate of alumina, as such and in its insoluble form, is added to the potassium meta or pyrophosphate or to a mixture of them, either during the process of melting or to the potassium phosphates in the phosphoric acid solution employed as a starting material, in 1 that a'solution of phosphoric acid contaminated with or rendered impure by alu minais employed in the production of the insoluble phosphates. Should the phosphate of alumina contain a small proportion of iron the latter is also converted into a soluble form.
In the production of potassium orthophos- 3 version take place, said conversion being completed in about two hours at a temperature of about 120 centigrade, the reaction being vsomewhat accelerated by addition of phos* phoric acid to the solution.
ble for use as fertilizers in that they contain potassium oxid and phosphoric acid and are therefore well adapted as substitutes for that :class of fertilizers which 'contain chemical combinations of potassium together with phosphatic constituents, and have the advantage over the latter fertilizers in that said products do not contain undesirable chlorids.
Having thus described my invention, what I claim as new therein, and desire to secure by Letters Patent, is
1. The herein-described processof obtain- 'ing meta or pyro-phosphoric acidcombina 'tions from phosphate salts of the metals of "thealkalies, which consists "inmelting the in soluble salt or salts and rapidly coolingthe same to prevent crystallization for the pur- {pose set forth. A
2; The herein described process'of' obtaining meta or pyro-phosphoric'acidcombinations, from phosphate salts of the metals of 5 the alkalies, which eonsistsin melting the insoluble salt together with a salt of the metals of the alkalies, and rapidly cooling the same to prevent crystallization for the purposeset forth.
HEINRICH PRECHT.
Witnesses:
EGGELING, E. KOHLE.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US502424A true US502424A (en) | 1893-08-01 |
Family
ID=2571261
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US502424D Expired - Lifetime US502424A (en) | Heinrich precht |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US502424A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3230040A (en) * | 1962-01-02 | 1966-01-18 | Monsanto Co | Trimetaphosphate processes |
| US3230039A (en) * | 1962-01-02 | 1966-01-18 | Monsanto Co | Process for manufacturing sodium trimetaphosphate products |
-
0
- US US502424D patent/US502424A/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3230040A (en) * | 1962-01-02 | 1966-01-18 | Monsanto Co | Trimetaphosphate processes |
| US3230039A (en) * | 1962-01-02 | 1966-01-18 | Monsanto Co | Process for manufacturing sodium trimetaphosphate products |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US3192013A (en) | Anhydrous liquid phosphoric acid | |
| US2288418A (en) | Manufacture of mixed phosphates | |
| US3361523A (en) | Method for producing phosphates | |
| US502424A (en) | Heinrich precht | |
| US2493809A (en) | Manufacture of polyphosphates | |
| US4777026A (en) | Production of phosphates from alkali-processes phosphate rock | |
| US3314750A (en) | Trimetaphosphate processes | |
| US1988991A (en) | Manufacture of solid products containing alkali hypochlorite | |
| US2962354A (en) | Method for producing condensed phosphatesalts | |
| US3241946A (en) | Ammonium phosphate fertilizer solids derived from anhydrous liquid phosphoric acid | |
| US3770410A (en) | Production of potassium polyphosphates from phosphate acid sludges | |
| US3243279A (en) | Ammonium phosphate solids derived from anhydrous liquid phosphoric acid | |
| NO780703L (en) | PROCEDURE FOR THE PREPARATION OF AN ALKALINE, GLOWED PHOSPHATE FERTILIZER | |
| US6656441B2 (en) | Process for the preparation of lithium metaphosphate | |
| US2423895A (en) | Method of production of anhydrous fluorophosphoric acid | |
| US3473889A (en) | Method for producing phosphates | |
| US836781A (en) | Process of obtaining lithium salts. | |
| US2111277A (en) | Process for reacting ammonium nitrate to form nitrous oxide | |
| US3347627A (en) | Process for manufacturing sodium trimetaphosphate | |
| US3414375A (en) | Two-stage process for the preparation of potassium metaphosphate | |
| NO145262B (en) | PROCEDURE FOR PREPARING A STABLE SOLUTION OF ERGOTAL KALOIDS OR THEIR SALTS | |
| US1270515A (en) | Process of producing potassium and phosphorus compounds. | |
| US2022050A (en) | Preparation of phosphoric acids | |
| US1636701A (en) | Process of manufacturing acetic anhydride | |
| US1852856A (en) | Process of producing cyanids |