DE894102C - Process for the production of disodium phosphate - Google Patents
Process for the production of disodium phosphateInfo
- Publication number
- DE894102C DE894102C DEC1572D DEC0001572D DE894102C DE 894102 C DE894102 C DE 894102C DE C1572 D DEC1572 D DE C1572D DE C0001572 D DEC0001572 D DE C0001572D DE 894102 C DE894102 C DE 894102C
- Authority
- DE
- Germany
- Prior art keywords
- phosphate
- production
- disodium phosphate
- solution
- trialkali
- 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
Links
- 239000001488 sodium phosphate Substances 0.000 title claims description 9
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 title claims description 7
- 235000019800 disodium phosphate Nutrition 0.000 title claims description 7
- 229910000397 disodium phosphate Inorganic materials 0.000 title claims description 6
- 238000000034 method Methods 0.000 title claims description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 9
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 8
- 229910019142 PO4 Inorganic materials 0.000 claims description 8
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 claims description 8
- 239000010452 phosphate Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 8
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 5
- 150000008065 acid anhydrides Chemical class 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 2
- 150000007513 acids Chemical class 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 239000007900 aqueous suspension Substances 0.000 claims 1
- 229910002090 carbon oxide Inorganic materials 0.000 claims 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 claims 1
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 6
- 235000021317 phosphate Nutrition 0.000 description 5
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 239000012452 mother liquor Substances 0.000 description 3
- 235000010265 sodium sulphite Nutrition 0.000 description 3
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 3
- 239000005457 ice water Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 230000008719 thickening Effects 0.000 description 2
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 2
- 235000019801 trisodium phosphate Nutrition 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-M Formate Chemical compound [O-]C=O BDAGIHXWWSANSR-UHFFFAOYSA-M 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 239000004280 Sodium formate Substances 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- LVXHNCUCBXIIPE-UHFFFAOYSA-L disodium;hydrogen phosphate;hydrate Chemical compound O.[Na+].[Na+].OP([O-])([O-])=O LVXHNCUCBXIIPE-UHFFFAOYSA-L 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- HLBBKKJFGFRGMU-UHFFFAOYSA-M sodium formate Chemical compound [Na+].[O-]C=O HLBBKKJFGFRGMU-UHFFFAOYSA-M 0.000 description 1
- 235000019254 sodium formate Nutrition 0.000 description 1
- 229910000162 sodium phosphate Inorganic materials 0.000 description 1
- 235000011008 sodium phosphates Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- C01B25/30—Alkali metal phosphates
- C01B25/308—Methods for converting an alkali metal orthophosphate into another one; Purification; Decolorasing; Dehydrating; Drying
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
Description
Verfahren zur Herstellung von Dinatriumphosphat Nach einem früher vorgeschlagenen Verfahren soll Dialkaliphosphat aus Trialkaliphosphat in der Weise hergestellt werden, daß man Kohlensäure in eine konzentrierte Lösung oder Suspension von Trialkaliphosphat unter Überdruck und bei normalen bis mäßig erhöhten Temperaturen, vorzugsweise unter 35°, so lange einleitet, bis ein pH-Wert, gemessen in 5o/oiger Lösung, erreicht ist, der über dem des Dialkaliphosphats und unter dem der Soda liegt.Process for the preparation of disodium phosphate According to an earlier proposed method is dialkali phosphate from trialkali phosphate in the manner can be prepared by adding carbonic acid to a concentrated solution or suspension of trialkali phosphate under excess pressure and at normal to moderately elevated temperatures, preferably below 35 °, introduced until a pH value measured in 5o / oiger Solution, which is above that of the dialkali phosphate and below that of the soda lies.
Es wurde gefunden, daß man an Stelle von Kohlensäure ganz allgemein solche gas- oder dampfförmigen Säureanhydride, die zur technischen Gewinnung ,der entsprechenden Säuren als billige Zwischenprodukte dienen, z. B. Kohlenoyxd, Stickoxyde, Schwefeldioxyd, zur Einleitung in die Trialkaliorthophosphatlösung benutzen kann. Der besondere Vorteil dieser Arbeitsweise liegt hierbei nicht allein darin, daß diese Säurean.hydride billig sind, sondern vor allem in dem Umstand, daß die hierbei anfallenden Nebenprodukte hochwertige Salze darstellen. So erhält man beispielsweise beim Arbeiten mit Kohlenoxyd, das in Form des billigen gereinigten Generatorgases benutzt werden kann, Alkaliformiat, beim Einleiten von Stickoxyd und Luft bzw. eines Gemisches von I NO mit N02 Alkalinitrat und bei Verwendung von Schwefeldioxyd Alkalisulfit.It has been found that in place of carbonic acid, in general those gaseous or vaporous acid anhydrides that are used for industrial production, the corresponding acids serve as cheap intermediates, e.g. B. carbon dioxide, nitrogen oxides, Sulfur dioxide, can be used to introduce into the trialkali orthophosphate solution. The particular advantage of this way of working is not only that These acid anhydrides are cheap, but mainly because they are resulting by-products represent high-quality salts. So you get for example when working with carbon monoxide in the form of cheap, purified generator gas can be used, alkali formate, when introducing nitrogen oxide and air or a Mixture of I NO with N02 alkali nitrate and, if sulfur dioxide is used, alkali sulfite.
Beispiel i In einem Rührautoklav werden iooo Volumteile einer wäßrigen Lösung von Trinatriumphosphat mit einem Gehalt von 24.o Gewichtsteilen Na. P O4 unter einem Druck von 35 bis q.o Atm. und bei einer Temperatur von etwa 16o° mit Kohlenmonoxyd behandelt. Nach 24. Stunden wird abgekühlt und das nicht umgesetzte Kohlenmonoxyd abgelassen. Die etwa 6o° warme, schwach alkalisch reagierende Lösung wird anschließend filtriert und unter Rühren auf etwa io° abgekühlt, wobei sich das entstandene Dinatriumphosphat als 12-Hydrat (Na. H P 04 - 12 H2 O) bis auf einen geringen Rest abscheidet. Man filtriert scharf ab und wäscht mit wenig Eiswasser nach. Der in der Lösung verbleibende Teil an Phosphat wird durch Eindicken der Mutterlauge und Abkühlen gewonnen. Als Hauptfraktion an Dinatriumphosphat erhält mär ein Feuchtprodukt mit 18,5 % P2 0S in einer Menge von 556 Gewichtsteilen. Es werden .in dieser Fraktion 98,81/o des eingesetzten P2 05 erhalten.Example i In a stirred autoclave, 100 parts by volume of an aqueous Solution of trisodium phosphate with a content of 24.o parts by weight N / A. P O4 under a pressure of 35 to q.o atm. and at a temperature of about 16o ° treated with carbon monoxide. After 24 hours it is cooled down and not released carbon monoxide. The approximately 60 ° warm, weakly alkaline reacting The solution is then filtered and cooled to about 10 ° with stirring, with the disodium phosphate formed as 12-hydrate (Na. H P 04 - 12 H2 O) to separates to a small residue. It is filtered sharply and washed with a little Ice water after. The part of the phosphate remaining in the solution is thickened won the mother liquor and cooling. Receives as the main fraction of disodium phosphate mär a moist product with 18.5% P2 0S in an amount of 556 parts by weight. It 98.81 / o of the P2 05 used are obtained in this fraction.
Aus der nach .der Abschei'dung der zweiten Fraktion von Dinatriumphosphat erhaltenen Mutterlauge erhält man nach :dem Eindicken. auf etwa Zoo Volurnteile das kristallisierte Natriumformiat in einer Ausbeute von 78 Gewichtsteilen =9311/o der Theorie. Beispiele In eine warme Lösung von 103 Gewichtsteilen Trinatriumphosphat (Na3 P O4) in 3.4o Volumteilen Wasser wird Schwefeldioxyd in feinverteilter Förm eingeleitet, bis ein pA von etwa 8,5 erreicht ist. Man läßt einige Stunden. bei möglichst niedriger Raumtemperatur stehen, filtriert und wäscht mit wenig Eiswasser. Die Ausbeute an kristallisiertem noch feuchtem Dinatriumphosphati2-Hydrat beträgt 2o5 Gewichtsteile bei einem P20. -Gehalt von r8,7%. Die Ausbringung an P20.. beträgt somit 97% des eingesetzten. Das Produkt enthält nur Spuren von Natriumsulfit und ist somit, praktisch reines krist. Di.natriumphosphat. Aus der Mutterlauge wird durch schwaches Eindicken zunächst der. Hauptanteil des noch in Lösung verbliebenen Dinatriumphosphates zusammen mit etwas Natriumsulfit krist. :gewonnen. Nach. dessen Abtrennung wird. stark eingedickt und das krist. Natriumsulfit in fst theoretischer Ausbeute gewonnen.From after the separation of the second fraction of disodium phosphate obtained mother liquor is obtained after: thickening. on about zoo volur parts the crystallized sodium formate in a yield of 78 parts by weight = 9311 / o the theory. Examples In a warm solution of 103 parts by weight of trisodium phosphate (Na3 P O4) in 3.4o parts by volume of water becomes sulfur dioxide in finely divided form initiated until a pA of approximately 8.5 is reached. One leaves a few hours. at Stand room temperature as low as possible, filter and wash with a little ice water. The yield of crystallized, still moist disodium phosphate hydrate is 2o5 parts by weight for a P20. -Content of r8.7%. The output at P20 .. is thus 97% of the used. The product contains only traces of sodium sulfite and is thus, practically pure crystal. Di sodium phosphate. The mother liquor becomes through weak thickening initially the. Main part of that still remaining in solution Disodium phosphates together with some sodium sulfite, crystalline. : won. To. whose Separation will. strongly thickened and the krist. Sodium sulfite in almost theoretical terms Yield gained.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEC1572D DE894102C (en) | 1944-04-09 | 1944-04-09 | Process for the production of disodium phosphate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEC1572D DE894102C (en) | 1944-04-09 | 1944-04-09 | Process for the production of disodium phosphate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE894102C true DE894102C (en) | 1953-10-22 |
Family
ID=7012642
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEC1572D Expired DE894102C (en) | 1944-04-09 | 1944-04-09 | Process for the production of disodium phosphate |
Country Status (1)
| Country | Link |
|---|---|
| DE (1) | DE894102C (en) |
-
1944
- 1944-04-09 DE DEC1572D patent/DE894102C/en not_active Expired
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