DE860487C - Process for the production of urea from carbon dioxide and ammonia - Google Patents
Process for the production of urea from carbon dioxide and ammoniaInfo
- Publication number
- DE860487C DE860487C DEP3097A DEP0003097A DE860487C DE 860487 C DE860487 C DE 860487C DE P3097 A DEP3097 A DE P3097A DE P0003097 A DEP0003097 A DE P0003097A DE 860487 C DE860487 C DE 860487C
- Authority
- DE
- Germany
- Prior art keywords
- urea
- carbon dioxide
- ammonia
- production
- gas
- 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims description 16
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 title claims description 10
- 239000004202 carbamide Substances 0.000 title claims description 10
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims description 8
- 239000001569 carbon dioxide Substances 0.000 title claims description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 title claims description 6
- 238000000034 method Methods 0.000 title claims description 4
- 229910021529 ammonia Inorganic materials 0.000 title claims description 3
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 239000007858 starting material Substances 0.000 claims description 2
- 150000002484 inorganic compounds Chemical class 0.000 claims 1
- 150000002898 organic sulfur compounds Chemical class 0.000 claims 1
- 239000007789 gas Substances 0.000 description 9
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 4
- IJCVBMSXIPFVLH-UHFFFAOYSA-N [C].S=O Chemical compound [C].S=O IJCVBMSXIPFVLH-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 229910000570 Cupronickel Inorganic materials 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 229910045601 alloy Inorganic materials 0.000 description 2
- 239000000956 alloy Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000003245 coal Substances 0.000 description 2
- YOCUPQPZWBBYIX-UHFFFAOYSA-N copper nickel Chemical compound [Ni].[Cu] YOCUPQPZWBBYIX-UHFFFAOYSA-N 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 150000003464 sulfur compounds Chemical class 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 206010007733 Catabolic state Diseases 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- -1 hydrogen sulphide Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C275/00—Derivatives of urea, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
- C07C275/04—Derivatives of urea, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups having nitrogen atoms of urea groups bound to acyclic carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C273/00—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups
- C07C273/02—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds
- C07C273/04—Preparation of urea or its derivatives, i.e. compounds containing any of the groups, the nitrogen atoms not being part of nitro or nitroso groups of urea, its salts, complexes or addition compounds from carbon dioxide and ammonia
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/141—Feedstock
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Carbon And Carbon Compounds (AREA)
- Treating Waste Gases (AREA)
Description
Bei der Synthese von Harnstoff durch Umsetzung von Kohlendioxyd und Ammoniak unter Druck in der Hitze besteht bekanntlich die Schwierigkeit, daß die Werkstoffe der Apparate starken Angriffen ausgesetzt und daher öfter erneuerungsbedürftig sind. Man sucht diesen Mängeln dadurch zu begegnen, daß man die gefährdeten Teile der Vorrichtung aus Spezialstählen, Kupfer-Nickel-Legierungen, Blei oder Silber herstellt oder sie damit auskleidet.In the synthesis of urea by converting carbon dioxide and ammonia under pressure in the As is well known, the problem with heat is that the materials of the apparatus are exposed to severe attack and are therefore in need of renewal more often. One tries to counteract these deficiencies by the Manufactures endangered parts of the device from special steels, copper-nickel alloys, lead or silver or lines them with it.
Es hat sich nun gezeigt, daß die Korrosion der Vorrichtung nicht lediglich auf das Reaktionsgemisch selbst zurückzuführen ist, sondern daß hierfür auch kleine Mengen von Verunreinigungen verantwortlich sind, die bei der Herstellung der Ausgangsstoffe nach den üblichen Verfahren nicht restlos entfernt werden, und es wurde gefunden, daß sich eine wesentliche Verbesserung der Haltbarkeit der Vorrichtung ergibt, wenn man nicht nur für die Fernhaltung von Sauerstoff sorgt, wie dies bereits früher vorgeschlagen worden ist, sondern wenn man die Ausgangsgase vor ihrer Umsetzung zu Harnstoff vor allem auch von Schwefelverbindungen sorgfältig befreit. Dabei ist es wichtig, außer anorganischen Schwefelverbindungen, wie Schwefelwasserstoff, auch den organisch gebun-It has now been shown that the corrosion of the device does not only affect the reaction mixture itself is due, but that this is also responsible for small amounts of impurities that are not completely removed during the production of the starting materials using the usual methods, and it has been found that there is a substantial improvement in the durability of the device, if you don't just keep oxygen out, as suggested earlier but if you consider the starting gases before they are converted into urea, especially from Sulfur compounds carefully freed. It is important, in addition to inorganic sulfur compounds, like hydrogen sulphide, also organically bound
denen Schwefel, insbesondere das Kohlenoxysulfid zu entfernen, das sich durchweg im Kohlendioxyd vorfindet, wenn dieses in der bekannten Weise durch katab/tische Umsetzung von Wassergas mit Wasserdampf gewonnen ist. Kohlenoxysulfid selbst gefährdet zwar nicht die hier in Frage kommenden Werkstoffe, wie Blei, Silber oder Kupfer-Nickel-Legierungen, es setzt sich aber, wie sich ergeben hat, unter den Bedingungen der Harnstoffsynthese zu dem schädlichen Schwefelwasserstoff um. Man findet nämlich in dem Reaktionsprodukt oder in den Abgasen der Harnstoffsynthese auch dann Schwefelwasserstoff, wenn man das Kohlendioxyd, vor der Umsetzung zu Harnstoff sorgfältig von Schwefelwasserstoff gereinigt hat, es sei denn, man hat im Sinn der vorliegenden Erfindung das auf Harnstoff zu verarbeitende Kohlendioxyd auch von Kohlenoxysulfid befreit.remove sulfur, especially carbon oxysulphide, which is always found in carbon dioxide, if this is done in the known manner by catabolic reaction of water gas with water vapor is won. Carbon oxysulphide itself does not endanger the materials in question here, like lead, silver or copper-nickel alloys, but, as it turned out, it settles under the conditions urea synthesis to the harmful hydrogen sulfide. One finds namely in that Reaction product or in the exhaust gases of urea synthesis also hydrogen sulfide, if one the carbon dioxide, before the conversion to urea, has carefully cleaned of hydrogen sulfide, it was because, in the sense of the present invention, the carbon dioxide to be processed on urea also has freed from carbon oxysulphide.
Man kann so verfahren, daß man das Kohlendioxydgas, nachdem es bereits unter dem für die Harnstoffsynthese erforderlichen Druck steht, zusammen mit Sauerstoff über eine aktive Kohle leitet, die nach dem Verfahren der Patentschrift 463 772 aus Steinkohle in der Weise hergestellt ist, daß man das auf einer Schicht feuerfesten Materials lagernde stückige oder (fein gekörnte zu aktivierende" Material mit Hilfe der heißen aktivierenden Gase ständig durchrührt. Durch Behandlung mit einer solchen aktiven Kohle verliert das Kohlendioxydgas den größten Teil seines Kohlenöxysulfidgehaltes. Leitet man das Gas dann in Gegenwart von Wasserdampf, der übliche Feuchtigkeitsgehalt des Gases reicht meistens aus, in der Hitze über schwefelaufnehmende, vorzugsweise Kupfer und Nickel enthaltende Massen, so wird auch der Rest des Kohlenoxysulfids entfernt, und das Gas kann dann der Harnstoffsynthese zugeführt werden. Ist nach der Behändlung des Gases mit der aktiven Kohle noch ein restlicher Sauerstoffgehalt vorhanden, so setzt sich dieser in der zweiten Stufe der Reinigung unter der katalytischen Wirkung der Reinigungsmasse mit den Wasserstoffbeimengungen, die das aus Wassergas gewonnene Kohlendioxyd meistens enthält, zu Wasser um, so daß das so gereinigte Gas auch von dem schädlichen Sauerstoff frei ist.One can proceed in such a way that the carbon dioxide gas, after it is already under the pressure required for the urea synthesis, is passed together with oxygen over an active carbon which is produced from hard coal according to the method of patent specification 463 772 in such a way that the Lumpy or ( finely grained to be activated) material stored on a layer of refractory material is constantly stirred with the aid of the hot activating gases. the usual moisture content of the gas is usually sufficient, in the heat over sulfur-absorbing, preferably copper and nickel-containing masses, so the rest of the carbon oxysulphide is also removed, and the gas can then be fed to the urea synthesis Coal still contains a remaining amount of oxygen If present, it is converted into water in the second stage of cleaning under the catalytic effect of the cleaning compound with the hydrogen admixtures which the carbon dioxide obtained from water gas usually contains, so that the gas thus cleaned is also free from harmful oxygen.
Claims (1)
Deutsche Patentschriften Nr. 299132, 537765;
Chem. Zentralblatt 1903,1,1053.Referred publications:
German Patent Nos. 299132, 537765;
Chem. Zentralblatt 1903,1,1053.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR860487X | 1946-11-15 |
Publications (1)
Publication Number | Publication Date |
---|---|
DE860487C true DE860487C (en) | 1952-12-22 |
Family
ID=9333921
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DEP3097A Expired DE860487C (en) | 1946-11-15 | 1948-10-02 | Process for the production of urea from carbon dioxide and ammonia |
Country Status (4)
Country | Link |
---|---|
BE (1) | BE491319A (en) |
CH (1) | CH284406A (en) |
DE (1) | DE860487C (en) |
FR (1) | FR1014334A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1015787B (en) * | 1953-01-21 | 1954-09-19 | Pechiney Prod Chimiques Sa | Process for the removal of oxygen admixtures from the gases used as starting material for the synthesis of urea |
DE953876C (en) * | 1953-04-15 | 1956-12-06 | Stamicarbon | Process for the production of urea |
DE1034617B (en) * | 1952-10-25 | 1958-07-24 | Chemical Construction Corp | Process for the production of urea |
US3354158A (en) * | 1964-12-23 | 1967-11-21 | Monsanto Co | Process improvements for preparing cyanuric acid |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE299132C (en) * | ||||
DE537765C (en) * | 1926-08-06 | 1931-11-12 | Alfons Klemenc Dr | Process for the production of urea from carbon oxysulphide and ammonia |
-
0
- BE BE491319D patent/BE491319A/xx unknown
-
1946
- 1946-11-15 FR FR1014334D patent/FR1014334A/en not_active Expired
-
1948
- 1948-10-02 DE DEP3097A patent/DE860487C/en not_active Expired
-
1949
- 1949-10-01 CH CH284406D patent/CH284406A/en unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE299132C (en) * | ||||
DE537765C (en) * | 1926-08-06 | 1931-11-12 | Alfons Klemenc Dr | Process for the production of urea from carbon oxysulphide and ammonia |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1034617B (en) * | 1952-10-25 | 1958-07-24 | Chemical Construction Corp | Process for the production of urea |
DE1015787B (en) * | 1953-01-21 | 1954-09-19 | Pechiney Prod Chimiques Sa | Process for the removal of oxygen admixtures from the gases used as starting material for the synthesis of urea |
DE953876C (en) * | 1953-04-15 | 1956-12-06 | Stamicarbon | Process for the production of urea |
US3354158A (en) * | 1964-12-23 | 1967-11-21 | Monsanto Co | Process improvements for preparing cyanuric acid |
Also Published As
Publication number | Publication date |
---|---|
BE491319A (en) | 1900-01-01 |
FR1014334A (en) | 1952-08-13 |
CH284406A (en) | 1952-07-31 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE860487C (en) | Process for the production of urea from carbon dioxide and ammonia | |
DE812547C (en) | Process for cleaning up carbon dioxide | |
DE736975C (en) | Process for the extraction of elemental sulfur from gases containing hydrogen sulfide, carbon oxysulfide and carbon disulfide | |
EP0277125B1 (en) | Process for removing volatile contents from waste liquids produced in coking plants | |
DE545368C (en) | Process for removing carbon oxysulphide from gases | |
DE1283208B (en) | Process for the separate production of ammonia and sulfur dioxide from the waste liquor produced in the production of methacrylic acid esters | |
DE535725C (en) | Process for the production of thiourea from metal cyanamides and sulfides by the action of carbonic acid | |
DEP0003097DA (en) | Process for the production of urea from carbon dioxide and ammonia | |
DE840391C (en) | Process for the production of a gas mixture suitable for urea synthesis from ammonia water | |
DE672414C (en) | Process for separating ammonia and hydrogen sulfide from distillation gases | |
DE712217C (en) | Manufacture of carbon disulfide | |
DE1216267B (en) | Process for the production of ammonia from carbon distillation gases in the form of diammonium phosphate | |
DE1029347B (en) | Process for cleaning the exhaust air from viscose factories | |
DE410866C (en) | Process for the utilization of gas cleaning compounds | |
DE931645C (en) | Process for the production of compressed, de-acidified ammonia water | |
DE393727C (en) | Process for removing sulfur compounds from gases | |
DE523520C (en) | Process for the production of thiourea | |
DE2638223A1 (en) | Sodamide mfr. for organic synthesis, e.g. indigo mfr. - in which ammonia is recycled to prevent pollution | |
DE566036C (en) | Process for the purification of crude hydrocarbon mixtures from hydrogen sulfide and hydrocyanic acid | |
DE583788C (en) | Extraction of oxygen | |
DE556457C (en) | Process for the production of rhodane compounds | |
DE386678C (en) | Process for separating organic gases and vapors | |
DE878639C (en) | Process for preventing corrosion in the deacidification of ammonia water | |
DE752219C (en) | Process for treating fish protein | |
DE415684C (en) | Process for the production of nitrogen-containing condensation products from acetylene and ammonia |