DE2106019A1 - Process for the preparation of sulfamic acid - Google Patents
Process for the preparation of sulfamic acidInfo
- Publication number
- DE2106019A1 DE2106019A1 DE19712106019 DE2106019A DE2106019A1 DE 2106019 A1 DE2106019 A1 DE 2106019A1 DE 19712106019 DE19712106019 DE 19712106019 DE 2106019 A DE2106019 A DE 2106019A DE 2106019 A1 DE2106019 A1 DE 2106019A1
- Authority
- DE
- Germany
- Prior art keywords
- reaction
- ammonia
- sulfamic acid
- acid
- preparation
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/087—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms
- C01B21/093—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms containing also one or more sulfur atoms
- C01B21/0935—Imidodisulfonic acid; Nitrilotrisulfonic acid; Salts thereof
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/087—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms
- C01B21/092—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms containing also one or more metal atoms
- C01B21/0923—Metal imides or amides
- C01B21/0926—Metal imides or amides of alkali metals
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B21/00—Nitrogen; Compounds thereof
- C01B21/082—Compounds containing nitrogen and non-metals and optionally metals
- C01B21/087—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms
- C01B21/093—Compounds containing nitrogen and non-metals and optionally metals containing one or more hydrogen atoms containing also one or more sulfur atoms
- C01B21/096—Amidosulfonic acid; Salts thereof
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
FARBWERKE HOECHST AKTIENGESELLSCHAFT
vormals Meister Lucius & BrüningFARBWERKE HOECHST AKTIENGESELLSCHAFT
formerly Master Lucius & Brüning
Datum: 8. Februar 1971 - Dr.BK/Ba Aktenzeichen: · - HOE 71/F Date: February 8, 1971 - Dr.BK / Ba File number: - HOE 71 / F
Verfahren zum Herstellen von AmidosulfonsäureProcess for the preparation of sulfamic acid
Gegenstand der Erfindung ist ein Verfahren zum Herstellen von Amidosulfonsäure durch Umsetzen von Schwefeltrioxid mit Ammoniak in der Gasphase und Hydrolyse des gebildeten Reaktionsgemischs mit Mineralsäure.The invention relates to a process for producing sulfamic acid by reacting sulfur trioxide with ammonia in the gas phase and hydrolysis of the reaction mixture formed with mineral acid.
Die Umsetzung von Schwefeltrioxid mit Ammoniak in·der Gasphase zu einem Gemisch der Ammoniumsalze von Schwefelsäure, Amidosulfonsäure, Imidodisulfonsäure und Nitrilotrisulfonsäure ist z. B. aus der deutschen Patentschrift 903 571 bekannt. Die Reaktionswärme muß dabei durch die Wand der Reaktionskammer abgeführt werden. Es ist ganz allgemein schwierig, bei Reaktionen, die aus der Gasphase unmittelbar zu einem Feststoff führen, die Wärme abzuführen. Besondere Schwierigkeiten ergeben sich bei der Reaktion zwischen Schwefeltrioxid und Ammoniak, die stark exotherm und momentan verläuft. Es besteht die Gefahr der Überhitzung, die die Bildung einer glasartigen Schmelze zur Folge hat, welche im wesentlichen nur aus Ammoniumsulfat und Ammoniumim'idodisulfonat besteht. Dadurch vermindert sich die Ausbeute an Amidosulfonsäure erheblich.The reaction of sulfur trioxide with ammonia in the gas phase to a mixture of the ammonium salts of sulfuric acid, sulfamic acid, imidodisulfonic acid and nitrilotrisulfonic acid is z. B. known from German patent specification 903 571. The heat of reaction must be discharged through the wall of the reaction chamber. In general, it is difficult with reactions that lead directly from the gas phase to a solid, dissipate the heat. Particular difficulties arise with the reaction between sulfur trioxide and ammonia, which is highly exothermic and momentary. There is a risk of overheating, which results in the formation of a glass-like melt, which essentially consists only of ammonium sulfate and ammonium im'idodisulfonate consists. This significantly reduces the yield of sulfamic acid.
'Zur Behebung dieser Mißstände ist schon vorgeschlagen worden (japanisches Patent 7515 (1951))» den Reaktionsraum in viele Einzelrohre zu gliedern, was aber einen hohen konstruktiven Aufwand bedingt. Die Wärme wird hier durch die Rohrwände abgeführt. 'Proposals have already been made to remedy these abuses (Japanese patent 7515 (1951)) »the reaction space in many To subdivide individual pipes, but this requires a high level of design effort. The heat is dissipated here through the pipe walls.
Nach einem anderen Vorschlag (japanisches Patent 1029 0952)) setzt man Schwefeltrioxid in starker Verdünnung mit Inertgas ein. Man bläst dabei ein Gasgemisch, das nur etwa 5 bis I5 % According to another proposal (Japanese patent 1029 0952), sulfur trioxide is used in strong dilution with inert gas. A gas mixture is blown that is only about 5 to 15 %
209835/0960 ./.209835/0960 ./.
'HOE 71/Ρ Ο48'HOE 71 / Ρ Ο48
SO„ enthält mit hoher Geschwindigkeit in gasförmiges Ammoniak. Die Reaktionswärme wird dabei zum Teil von dem Inertgas aufgenommen und durch die Reaktorwand abgeführt.SO “contains gaseous ammonia at high speed. The heat of reaction is partly absorbed by the inert gas and dissipated through the reactor wall.
Es wurde nun gefunden, daß man die Nachteile der bekannten Umsetzung von Schwefeltrioxid mit Ammoniak in der Gasphase vermeiden kann. , wenn man das Ammoniak wenigstens zum Teil in flüssiger Form in den Reaktionsraum bringt.It has now been found that the disadvantages of the known reaction of sulfur trioxide with ammonia in the gas phase are eliminated can avoid. , if you bring the ammonia at least partially in liquid form into the reaction chamber.
Die Reaktionswärme wird in diesem Fall unmittelbar als Verdampfungswärme durch das flüssige Ammoniak abgeführt. Im Gegen-r satz zum reinen Gasphasen__verfahren läßt sich die Temperatur über den Anteil an fein verteilt eingegebenem flüssigem Ammoniak sehr genau steuern. Außerdem kann die Raum-Zeit-Ausbeute gegenüber der reinen Gasphasenreaktion und erst recht gegenüber der Durchführung der Reaktion in Gegenwart eines Inertgases erheblich gesteigert werden. Bereits in einem konventionellen Reaktor erhält man bei Einsatz von flüssigem Ammoniak ohne weiteres die doppelte Raum-Zeit-Ausbeute gegenüber dem Einsatz von gasförmigem Ammoniak.In this case, the heat of reaction is used directly as the heat of evaporation dissipated by the liquid ammonia. In contrast to the pure gas phase process, the temperature Control very precisely the proportion of finely divided liquid ammonia added. In addition, the space-time yield compared to the pure gas phase reaction and even more so compared to carrying out the reaction in the presence of a Inert gas can be increased significantly. Even in a conventional reactor you get when using liquid Ammonia easily doubles the space-time yield compared to the use of gaseous ammonia.
3 In einen vorgegebenen Reaktor von 3» 2 m Inhalt werden pro Stunde 14,5 kg SO_ und 11,0 kg NH„ gasförmig eindosiert. Es entstehen pro Stunde 20 kg eines Reaktionsgemisches aus 32 $ Ammoniumamidosulf ona t, 58 $ Ammoniumimidodisulfonat und 10 $ Ammoniumsulfat.3 In a given reactor with a volume of 3 »2 m, pro Hour 14.5 kg SO_ and 11.0 kg NH "metered in in gaseous form. There are 20 kg per hour of a reaction mixture of 32 $ ammonium amido sulfonate, 58 $ ammonium imidodisulfonate and 10 $ ammonium sulfate.
In denselben Reaktor wie im Beispiel 1 wurden pro Stunde 28,8 kg S0_ und 30,0 kg NH„, das im wesentlichen flüssig war, eindosiert« Es entstanden pro Stunde kO kg eines Reaktbnsgemisches von gleicher Zusammensetzung wie im Beispiel 1, d. h., die Raum-Zeit-Ausbeute war doppelt so groß.In the same reactor as in Example 1 were 28.8 kg and 30.0 kg per hour s0_ NH "which was essentially liquid," metered It emerged per hour kO kg of Reaktbnsgemisches of the same composition as in Example 1, ie, the The space-time yield was twice as large.
209835/096D209835 / 096D
HOE 71/F 0^8 — 3 —HOE 71 / F 0 ^ 8 - 3 -
Von den Reaktionsgemischen aus den beiden Beispielen wurden je 120 g mit je 25O ml 60$iger Salpetersäure bei 6O° C hydrolysiert. Dann wurde auf 0 C gekühlt, und der gebildete Niederschlag wurde filtriert und mit 6O$iger Salpetersäure von O C gewaschen. Es wurde dann bei fO C getrocknet ;in beiden wurden ca. 60 g Amidosulfonsäure mit einem Gehalt von ca. 99»5 i° erhalten.120 g of the reaction mixtures from the two examples were hydrolyzed at 60 ° C. with 250 ml of 60% nitric acid each time. The mixture was then cooled to 0 C and the precipitate formed was filtered and washed with 60% strength nitric acid from OC. It was then dried at 50 ° C. In both, about 60 g of sulfamic acid with a content of about 99-5 ° were obtained.
209835/0960209835/0960
Claims (1)
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19712106019 DE2106019A1 (en) | 1971-02-09 | 1971-02-09 | Process for the preparation of sulfamic acid |
IT2029972A IT950691B (en) | 1971-02-09 | 1972-02-07 | PROCESS FOR THE PREPARATION OF AMIDOSULFONIC ACID |
FR7204291A FR2124590A1 (en) | 1971-02-09 | 1972-02-09 | Amidosulphonic acid prepn - from gaseous sulphur trioxide and partly liquid ammonia with subsequent mineral acid hydro |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19712106019 DE2106019A1 (en) | 1971-02-09 | 1971-02-09 | Process for the preparation of sulfamic acid |
Publications (1)
Publication Number | Publication Date |
---|---|
DE2106019A1 true DE2106019A1 (en) | 1972-08-24 |
Family
ID=5798220
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DE19712106019 Pending DE2106019A1 (en) | 1971-02-09 | 1971-02-09 | Process for the preparation of sulfamic acid |
Country Status (3)
Country | Link |
---|---|
DE (1) | DE2106019A1 (en) |
FR (1) | FR2124590A1 (en) |
IT (1) | IT950691B (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362790A1 (en) * | 1976-08-24 | 1978-03-24 | Hoechst Ag | PROCESS FOR THE PREPARATION OF AMIDOSULPHONIC ACID |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2710399C3 (en) * | 1977-03-10 | 1981-08-20 | Hoechst Ag, 6000 Frankfurt | Process for the production of ammonium sulfamate |
DE2850903A1 (en) * | 1978-11-24 | 1980-06-04 | Hoechst Ag | METHOD FOR PRODUCING AMMONIUM SULFAMATE |
-
1971
- 1971-02-09 DE DE19712106019 patent/DE2106019A1/en active Pending
-
1972
- 1972-02-07 IT IT2029972A patent/IT950691B/en active
- 1972-02-09 FR FR7204291A patent/FR2124590A1/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2362790A1 (en) * | 1976-08-24 | 1978-03-24 | Hoechst Ag | PROCESS FOR THE PREPARATION OF AMIDOSULPHONIC ACID |
US4107279A (en) * | 1976-08-24 | 1978-08-15 | Hoechst Aktiengesellschaft | Process for the preparation of amidosulfonic acid |
Also Published As
Publication number | Publication date |
---|---|
FR2124590A1 (en) | 1972-09-22 |
IT950691B (en) | 1973-06-20 |
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