AT70830B - Process for the production of urea. - Google Patents
Process for the production of urea.Info
- Publication number
- AT70830B AT70830B AT70830DA AT70830B AT 70830 B AT70830 B AT 70830B AT 70830D A AT70830D A AT 70830DA AT 70830 B AT70830 B AT 70830B
- Authority
- AT
- Austria
- Prior art keywords
- urea
- distillation
- production
- ammonia
- carbonic acid
- Prior art date
Links
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 title claims description 8
- 239000004202 carbamide Substances 0.000 title claims description 8
- 238000000034 method Methods 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title description 2
- 238000004821 distillation Methods 0.000 claims description 4
- 239000011541 reaction mixture Substances 0.000 claims description 3
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims description 2
- GBXLGOIRHPEOCR-UHFFFAOYSA-N C(N)([O-])=O.[NH4+].C([O-])([O-])=O.[NH4+].[NH4+] Chemical compound C(N)([O-])=O.[NH4+].C([O-])([O-])=O.[NH4+].[NH4+] GBXLGOIRHPEOCR-UHFFFAOYSA-N 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 6
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 229910021529 ammonia Inorganic materials 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 150000003863 ammonium salts Chemical class 0.000 description 2
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 235000012501 ammonium carbonate Nutrition 0.000 description 1
- 239000001099 ammonium carbonate Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- -1 petroleum or benzene Chemical class 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
<Desc/Clms Page number 1>
Verfahren zur Gewinnung von Harnstoff.
EMI1.1
salzen und Wasser entstehen. Arbeitet man dieses Reaktionsgemisch wie beschrieben in der Weise auf, dass man dasselbe nach d@@ Abkühlen mit W@@er aufnimmt und eindampft, so geht nicht nur das ganze Ammoniak verloren, sondern es treten mehr oder weniger grosse Harnstoffverluste auf.
Es hat sich nun gezeigt, dass eine nahezu quantitative Gewinnung des gebildeten Harnstoffs und zugleich eine völlige Wiedergewinnung der nicht umgesetzten Ammoniumsalze möglich ist, wenn man das Reaktionsgemisch einer Destillation bei 800 nicht wesentlich übersteigenden Temperaturen unterwirft. Man kann so arbeiten, dass die Ammoniumsalze unmittelbar in fester Form gewonnen werden können, während eine Lösung bzw. ein Brei von Harnstoff zurückbleibt, der gegebenenfalls durch weitere Destination unterhalb 800, zweckmässig unter vermindertem Dtuck in trockene Form gebracht werden kann. Man kann auch von Anfang an mit vermindertem Druck arbeiten- dans Verfahren wird z.
B. in folgender Weise ausgeführt:
EMI1.2
setzung vollzogen ist, durch ein unten benndtiches Auslassventil unter Entspannung langsam in einen Destillierbehälter eintreten, der mit einer Vorlage verbunden ist. Man kann hiebei den Destillierbehälter entweder anfangs kühl halten und erst nachträglich erforderlichenfalls bis auf etwa 75 heizen, oder man kann auch dafür sorgen, dass von Anfang an, z. B. eine Temperatur von 60 bis 70 im Destillierkessel vorhanden ist. Es entweichen Kohlensäure und Ammoniak, die sich in der Vorlage bzw. in darin befindlichen gekühlten Rohren oder dgl. als festes Karbarninat bzw. Karbonat verdichten, während im Ke. sse) praktisch nur Harnstoff und Wasser zurückbleiben.
Will man jenen in trockener Form gewinnen. h0 erwärmt man woter nach Wechsel der Vorlage oder in einem besonderen Apparat unter vermindertem Druck.
Eine zweckmässige Ausführungsform besteht darin. dass das beim Abdestillieren entweichende Gemisch von Ammoniak und Kohlensäure vorteilhaft unter Kählung in mit Wasser nicht mischbare. indifferente Flüssigkeiten, namentlich Kohlenwasserstoffe, wie Petroleum oder Benzol usw., eingeleitet wird. Die beiden Gase vereinigen sich auf diese Weise leicht zu festem Ammoniumkatbaminat. das gegebenenfalls Ammoniumkarbonat enthält.
EMI1.3
wieder verwendbar ist, trennen nnd direkt wieder in Harnstoff überführen, der dann gemäss dem oben beschriebenen Verfahren gewonnen wird.
**WARNUNG** Ende DESC Feld kannt Anfang CLMS uberlappen**.
<Desc / Clms Page number 1>
Process for the production of urea.
EMI1.1
salt and water arise. If this reaction mixture is worked up as described in such a way that it is taken up after d @@ cooling with W @@ er and evaporated, not only is all the ammonia lost, but more or less large urea losses occur.
It has now been shown that an almost quantitative recovery of the urea formed and at the same time a complete recovery of the unreacted ammonium salts is possible if the reaction mixture is subjected to a distillation at temperatures which do not significantly exceed 800. One can work so that the ammonium salts can be obtained directly in solid form, while a solution or a slurry of urea remains, which can optionally be brought into dry form by further destinations below 800, advantageously under reduced pressure. It is also possible to work with reduced pressure right from the start.
B. carried out in the following way:
EMI1.2
is complete, slowly enter a still through an outlet valve below, while releasing pressure, which is connected to a receiver. You can either keep the still cool at the beginning and only subsequently heat it up to about 75 if necessary, or you can also ensure that from the beginning, e.g. B. a temperature of 60 to 70 is present in the still. Carbonic acid and ammonia escape and condense as solid carbinate or carbonate in the template or in the cooled pipes or the like located therein, while in the Ke. sse) practically only urea and water remain.
If you want to win that in dry form. h0 is heated woter after changing the template or in a special apparatus under reduced pressure.
An expedient embodiment consists in this. that the mixture of ammonia and carbonic acid escaping during distillation is advantageously immiscible with water while cooling. inert liquids, namely hydrocarbons, such as petroleum or benzene, etc., is introduced. In this way, the two gases easily combine to form solid ammonium catamine. which optionally contains ammonium carbonate.
EMI1.3
can be reused, separate and convert directly back into urea, which is then obtained according to the method described above.
** WARNING ** End of DESC field may overlap beginning of CLMS **.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE70830X | 1914-02-13 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AT70830B true AT70830B (en) | 1915-12-27 |
Family
ID=5635584
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AT70830D AT70830B (en) | 1914-02-13 | 1914-12-21 | Process for the production of urea. |
Country Status (1)
| Country | Link |
|---|---|
| AT (1) | AT70830B (en) |
-
1914
- 1914-12-21 AT AT70830D patent/AT70830B/en active
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