DE292530C - - Google Patents
Info
- Publication number
- DE292530C DE292530C DENDAT292530D DE292530DA DE292530C DE 292530 C DE292530 C DE 292530C DE NDAT292530 D DENDAT292530 D DE NDAT292530D DE 292530D A DE292530D A DE 292530DA DE 292530 C DE292530 C DE 292530C
- Authority
- DE
- Germany
- Prior art keywords
- phosphoric acid
- ammonia
- sulfuric acid
- monobasic
- salt
- 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.)
- Active
Links
- NBIIXXVUZAFLBC-UHFFFAOYSA-N phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 34
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 17
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 13
- LFVGISIMTYGQHF-UHFFFAOYSA-N Ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims description 10
- 150000003839 salts Chemical class 0.000 claims description 8
- 239000011780 sodium chloride Substances 0.000 claims description 8
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 238000000034 method Methods 0.000 claims description 6
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000005712 crystallization Effects 0.000 claims description 3
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 3
- 238000005755 formation reaction Methods 0.000 claims description 3
- 239000003337 fertilizer Substances 0.000 claims description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims 3
- 235000011121 sodium hydroxide Nutrition 0.000 claims 3
- 239000002426 superphosphate Substances 0.000 claims 3
- 229940116349 Dibasic Ammonium Phosphate Drugs 0.000 claims 2
- YYRMJZQKEFZXMX-UHFFFAOYSA-N calcium;phosphoric acid Chemical compound [Ca+2].OP(O)(O)=O.OP(O)(O)=O YYRMJZQKEFZXMX-UHFFFAOYSA-N 0.000 claims 2
- 238000006243 chemical reaction Methods 0.000 claims 2
- BIGPRXCJEDHCLP-UHFFFAOYSA-N Ammonium bisulfate Chemical compound [NH4+].OS([O-])(=O)=O BIGPRXCJEDHCLP-UHFFFAOYSA-N 0.000 claims 1
- STZCRXQWRGQSJD-GEEYTBSJSA-M Methyl orange Chemical compound [Na+].C1=CC(N(C)C)=CC=C1\N=N\C1=CC=C(S([O-])(=O)=O)C=C1 STZCRXQWRGQSJD-GEEYTBSJSA-M 0.000 claims 1
- 229940012189 Methyl orange Drugs 0.000 claims 1
- 238000010521 absorption reaction Methods 0.000 claims 1
- 230000002378 acidificating Effects 0.000 claims 1
- -1 ammonia superphosphates Chemical class 0.000 claims 1
- 238000004043 dyeing Methods 0.000 claims 1
- 238000000605 extraction Methods 0.000 claims 1
- 238000005470 impregnation Methods 0.000 claims 1
- 239000000203 mixture Substances 0.000 claims 1
- 235000021317 phosphate Nutrition 0.000 claims 1
- 239000002367 phosphate rock Substances 0.000 claims 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 claims 1
- 239000011435 rock Substances 0.000 claims 1
- 238000004642 transportation engineering Methods 0.000 claims 1
- 239000002023 wood Substances 0.000 claims 1
- VHUUQVKOLVNVRT-UHFFFAOYSA-N ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000004254 Ammonium phosphate Substances 0.000 description 1
- 230000036826 Excretion Effects 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910000148 ammonium phosphate Inorganic materials 0.000 description 1
- 235000019289 ammonium phosphates Nutrition 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000029142 excretion Effects 0.000 description 1
- 230000000737 periodic Effects 0.000 description 1
- 238000000926 separation method Methods 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
- C01B25/28—Ammonium phosphates
-
- 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
- C01B25/40—Polyphosphates
- C01B25/405—Polyphosphates of ammonium
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Fertilizers (AREA)
Description
KAISERLICHESIMPERIAL
PATENTAMT,-PATENT OFFICE, -
Es gibt theoretisch drei verschiedene Ammoniumsalze der Phosphorsäure, von denen aber nur das primäre Salz NH1H2PO4 beständig ist, während die beiden anderen sich unter Abgäbe von Ammoniak allmählich in das einbasische Salz verwandeln.There are theoretically three different ammonium salts of phosphoric acid, of which only the primary salt NH 1 H 2 PO 4 is stable, while the other two gradually transform into the monobasic salt with the release of ammonia.
Die Herstellung von phosphorsaurem Ammoniak findet bisher in sehr geringem Umfange statt. Die naheliegende Verwendung desselbenThe production of phosphoric acid ammonia has so far been carried out on a very small scale instead of. The obvious use of the same
ίο als ein höchstkonzentriertes Düngemittel ist an seinem hohen Preise gescheitert; es findet bisher nur Verwendung zum Feuersichermachen brennbarer Stoffe usw. Durch die Herstellung dieses Produktes an den Produktionsstätten des Ammoniaks kann sein Preis, wie im folgenden des näheren dargelegt wird, ganz bedeutend reduziert werden, es fehlte aber noch an einem brauchbaren Fabrikations verfahren. Das bisherige Verfahren der rein empirischen Absätti- gung der Phosphorsäure mittels Ammoniakgas oder auch Ammoniakwasser ist für einen kontinuierlichen Betrieb unbrauchbar, es ist auch unrationell, weil das erzielte Produkt Ammoniakverluste erleidet, und vor allem, weil eine Ab-Scheidung des Salzes in heißer konzentrierter Lösung nicht stattfindet, sondern hierzu die gesättigte Lösung erst zum Erkalten gebracht werden muß.ίο as a highly concentrated fertilizer is on failed its high prices; so far it has only been used to make flammable fires safe Substances etc. Through the manufacture of this product at the ammonia production facilities its price can be reduced quite significantly, as will be explained in more detail below but a usable manufacturing process was still lacking. The previous method of purely empirical saturation supply of phosphoric acid by means of ammonia gas or ammonia water is for a continuous Operation unusable, it is also inefficient because the product obtained loses ammonia suffers, and mainly because a separation of the salt in hotter concentrated Solution does not take place, but for this the saturated solution is first brought to cool must become.
Man verfährt bisher einfach in der Weise, daß man eine unbestimmte Menge Phosphorsäure mit Ammoniak neutralisiert, bis die heiße gesättigte Lösung beim Erkalten zu einer Kristallmasse erstarrt. Da man nicht wußte, daß der Grad der Absättigung eine große Rolle auf den Prozeß ausübt, so hat man auch keinen Wert darauf gelegt und es vollständig dem Zufall überlassen, wie weit die Absättigung getrieben wurde.So far, the simple procedure is that an indefinite amount of phosphoric acid is used neutralized with ammonia until the hot saturated solution turns into a crystal mass on cooling stiffens. Not knowing that the degree of saturation played a major role Process, no value was attached to it and it was entirely a matter of chance up to how far the saturation was taken.
Der bisherige Prozeß ist naturgemäß ein periodischer. Sobald ein Bad gesättigt ist, muß es abgelassen und wieder mit neuen Mengen Phosphorsäure beschickt werden.The previous process is of course a periodic one. Once a bath is saturated, it must it can be drained and refilled with new amounts of phosphoric acid.
Es hat sich nun gezeigt, daß Lösungen, deren Absättigung mit Ammoniak so weit getrieben worden war, daß sie größere Mengen zweibasi- +5 sehen phosphorsauren Ammoniaks enthielten, selbst beim Erkalten, geschweige denn in der Hitze, keine oder nur eine unbedeutende Neigung zum Kristallisieren haben. Der Grund hierfür liegt in der Eigenschaft des zweibasischen phosphor sauren Ammoniaks, nicht nur selbst nicht zu kristallisieren, sondern auch die Kristallisation des an sich sehr leicht und sehr schön kristallisierenden einbasischen Salzes zu verhindern. .It has now been shown that solutions whose saturation with ammonia is carried so far had been that they had larger amounts dibasic +5 see phosphoric acid ammonia contained, even when cooling, let alone in the Heat, have little or no tendency to crystallize. The reason this lies in the property of the dibasic phosphoric acid ammonia, not just itself not to crystallize, but also the crystallization of the in itself very easy and very beautiful to prevent crystallizing monobasic salt. .
In Gemäßheit der vorliegenden Erfindung werden alle diese Schwierigkeiten umgangen und ein haltbares Ammoniumphosphat in kontinuierlichem Verfahren dadurch ermöglicht, daß man Phosphorsäure in kontinuierlichem Strome der bereits mit Ammoniak übersättigten Lauge zufließen läßt. Hierdurch wird eine momentane Ausscheidung des einbasischen Ammoniumphosphates in kristallinischer Form erzielt.In accordance with the present invention, all of these difficulties are circumvented and a durable ammonium phosphate made possible in a continuous process by the fact that Phosphoric acid flow in a continuous stream of the liquor already supersaturated with ammonia leaves. This causes a momentary excretion of the monobasic ammonium phosphate obtained in crystalline form.
Die Ausführung des Verfahrens erfolgt auf folgende Weise. In einen Ammoniakabsorptionsapparat, wie sie in allgemeiner Verwendung · sind, läßt man Phosphorsäure einfließen, während gleichzeitig Ammoniakgas oder -wasser durchströmt. Die Absättigung darf nur so weit getrieben werden, bis die Bildung des zweibasischen phosphorsauren Ammoniaks soebenThe procedure is carried out in the following manner. In an ammonia absorber, as they are in general use, phosphoric acid is allowed to flow in while ammonia gas or water flows through at the same time. The saturation is only allowed so far be driven until the formation of the dibasic phosphoric acid ammonia has just occurred
Claims (1)
Publications (1)
Publication Number | Publication Date |
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DE292530C true DE292530C (en) |
Family
ID=547286
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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DENDAT292530D Active DE292530C (en) |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE292530C (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1051871B (en) * | 1954-04-30 | 1959-03-05 | Dorr Oliver Inc | Continuous process for the production of high-quality, free-flowing, granulated diammonium phosphate fertilizers |
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0
- DE DENDAT292530D patent/DE292530C/de active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1051871B (en) * | 1954-04-30 | 1959-03-05 | Dorr Oliver Inc | Continuous process for the production of high-quality, free-flowing, granulated diammonium phosphate fertilizers |
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