DE1251900B - Process for removing nitrogen compounds from gases - Google Patents
Process for removing nitrogen compounds from gasesInfo
- Publication number
- DE1251900B DE1251900B DENDAT1251900D DE1251900DA DE1251900B DE 1251900 B DE1251900 B DE 1251900B DE NDAT1251900 D DENDAT1251900 D DE NDAT1251900D DE 1251900D A DE1251900D A DE 1251900DA DE 1251900 B DE1251900 B DE 1251900B
- Authority
- DE
- Germany
- Prior art keywords
- gases
- nitrogen compounds
- gas
- washing solution
- nitrogen
- 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
- 239000007789 gas Substances 0.000 title claims description 31
- 150000002830 nitrogen compounds Chemical class 0.000 title claims description 13
- 238000000034 method Methods 0.000 title claims 2
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 20
- 239000000243 solution Substances 0.000 claims description 16
- 238000005406 washing Methods 0.000 claims description 15
- LELOWRISYMNNSU-UHFFFAOYSA-N Hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 claims description 13
- 229910052813 nitrogen oxide Inorganic materials 0.000 claims description 6
- -1 Chelate complex compound Chemical class 0.000 claims description 5
- 150000002500 ions Chemical class 0.000 claims description 5
- KXDHJXZQYSOELW-UHFFFAOYSA-N carbamate Chemical class NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 claims description 4
- 150000001450 anions Chemical class 0.000 claims description 3
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 150000001735 carboxylic acids Chemical class 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 230000000737 periodic Effects 0.000 claims description 2
- 229910001385 heavy metal Inorganic materials 0.000 claims 1
- 238000005201 scrubbing Methods 0.000 claims 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 6
- 239000011780 sodium chloride Substances 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 238000002386 leaching Methods 0.000 description 5
- 150000004697 chelate complex Chemical class 0.000 description 4
- KCXVZYZYPLLWCC-UHFFFAOYSA-N edta Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 125000002843 carboxylic acid group Chemical group 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- 229920000591 gum Polymers 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 125000004433 nitrogen atoms Chemical group N* 0.000 description 2
- 125000004430 oxygen atoms Chemical group O* 0.000 description 2
- 125000004434 sulfur atoms Chemical group 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- CCVYRRGZDBSHFU-UHFFFAOYSA-N (2-hydroxyphenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC=C1O CCVYRRGZDBSHFU-UHFFFAOYSA-N 0.000 description 1
- AOHJOMMDDJHIJH-UHFFFAOYSA-N 1,2-Diaminopropane Chemical compound CC(N)CN AOHJOMMDDJHIJH-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N 1,2-ethanediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- GQBWTAGIANQVGB-UHFFFAOYSA-N 2-[N-(carboxymethyl)anilino]acetic acid Chemical compound OC(=O)CN(CC(O)=O)C1=CC=CC=C1 GQBWTAGIANQVGB-UHFFFAOYSA-N 0.000 description 1
- QDHGQJQZPJPKJK-UHFFFAOYSA-N 2-[carboxymethyl-(2,4,6-trioxo-1,3-diazinan-5-yl)amino]acetic acid Chemical compound OC(=O)CN(CC(O)=O)C1C(=O)NC(=O)NC1=O QDHGQJQZPJPKJK-UHFFFAOYSA-N 0.000 description 1
- JLAVVTDAVBLNJO-UHFFFAOYSA-N CC(O)=O.CC(O)=O.CC(O)=O.CC(O)=O.NC(N)COCC(N)N Chemical compound CC(O)=O.CC(O)=O.CC(O)=O.CC(O)=O.NC(N)COCC(N)N JLAVVTDAVBLNJO-UHFFFAOYSA-N 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N DETA Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 1
- OTBHHUPVCYLGQO-UHFFFAOYSA-N Norspermidine Chemical compound NCCCNCCCN OTBHHUPVCYLGQO-UHFFFAOYSA-N 0.000 description 1
- 229960003330 Pentetic Acid Drugs 0.000 description 1
- 229920002873 Polyethylenimine Polymers 0.000 description 1
- VILCJCGEZXAXTO-UHFFFAOYSA-N Triethylenetetramine Chemical compound NCCNCCNCCN VILCJCGEZXAXTO-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- KAKZBPTYRLMSJV-UHFFFAOYSA-N butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000003247 decreasing Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 230000001627 detrimental Effects 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- DEFVIWRASFVYLL-UHFFFAOYSA-N ethylene glycol bis(2-aminoethyl)tetraacetic acid Chemical compound OC(=O)CN(CC(O)=O)CCOCCOCCN(CC(O)=O)CC(O)=O DEFVIWRASFVYLL-UHFFFAOYSA-N 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atoms Chemical class [H]* 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000001771 impaired Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 125000000962 organic group Chemical group 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000010405 reoxidation reaction Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing Effects 0.000 description 1
- FAGUFWYHJQFNRV-UHFFFAOYSA-N tetraethylenepentamine Chemical compound NCCNCCNCCNCCN FAGUFWYHJQFNRV-UHFFFAOYSA-N 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10K—PURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
- C10K1/00—Purifying combustible gases containing carbon monoxide
- C10K1/08—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors
- C10K1/10—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids
- C10K1/12—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors
- C10K1/124—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors containing metal compounds other than alkali- or earth-alkali carbonates, hydroxides- or oxides- or salts of inorganic acids derived from sulfur
- C10K1/125—Purifying combustible gases containing carbon monoxide by washing with liquids; Reviving the used wash liquors with aqueous liquids alkaline-reacting including the revival of the used wash liquors containing metal compounds other than alkali- or earth-alkali carbonates, hydroxides- or oxides- or salts of inorganic acids derived from sulfur containing Fe compounds
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Environmental & Geological Engineering (AREA)
- Analytical Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Combustion & Propulsion (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Treating Waste Gases (AREA)
- Gas Separation By Absorption (AREA)
Description
DEUTSCHESGERMAN
PATENTAMTPATENT OFFICE
0 MITGL.. 00 MIT ... 0
Int CL: Int CL:
ClOkClOk
Deutsche Kl.: 26 d- 9/01 German class: 26 d- 9/01
Nummer:
Aktenzeichen:
Anmeldetag:
Auslegetag:Number:
File number:
Registration date:
Display day:
1251900
K49240IVc/26d
20. März 1963
12. Oktober 19671251900
K49240IVc / 26d
March 20, 1963
October 12, 1967
LAENDERCOUNTRIES
Die vorliegende Erfindung betrifft ein Verfahren zur Entfernung von Stickstoffverbindungen (Blausäure, Stickoxyd) aus Gasen mittels eines Waschprozesses. The present invention relates to a method for removing nitrogen compounds (hydrocyanic acid, Nitrogen oxide) from gases by means of a washing process.
Es gibt zahlreiche technische Gase, z. B. Synthesegas, Wassergas, Generatorgas, Kohlendestillationsgas u. dgl., die neben den erwünschten Bestandteilen auch Stickstoffverbindungen· als Verunreinigungen enthalten, vor allem Blausäure und Stickoxyd. Diese Stickstoffverbindungen neigen zusammen mit anderen Bestandteilen des Gases, insbesondere zusammen mit ungesättigten Kohlenwasserstoffen, zur Gumbildung, wodurch die Kompression solcher Gase sehr erschwert, häufig sogar unmöglich gemacht wird. Ferner wird durch die Gumbildung das einwandfreie Funktionieren der in den Gasleitungen installierten Meß- und Regelgeräte beeinträchtigt.There are numerous technical gases, e.g. B. synthesis gas, water gas, generator gas, coal distillation gas and the like, which in addition to the desired components also contain nitrogen compounds as impurities, especially hydrogen cyanide and nitrogen oxide. These nitrogen compounds tend to work along with other ingredients of the gas, especially together with unsaturated hydrocarbons, for gum formation, whereby the compression of such gases is made very difficult, often even impossible. Further the gum formation ensures the proper functioning of the measuring devices installed in the gas pipes and control devices impaired.
Die bisher gemachten Anstrengungen zur Entfernung von Stickstoffverbindungen aus Gasen, obwohl technisch im großen und ganzen erfolgreich, befriedigen jedoch nicht, weil wegen eines vergleichsweise großen Aufwandes an Waschmittel (meist alkalisiertes Wasser) oder an Apparaten (elektrisches Büschelfeld; Bestrahlungslampen) eine dem beschränkten Erfolg nicht entsprechende Verteuerung des gereinigten Gases eintritt.Efforts so far made to remove nitrogen compounds from gases, though technically successful by and large, but not satisfactory because of one thing in comparison large amount of detergent (mostly alkalized water) or equipment (electrical tuft field; Radiation lamps) an increase in the price of the cleaned one that does not correspond to the limited success Gas enters.
Die Erfindung hat sich zur Aufgabe gestellt, die Entfernung der Stickstoffverbindungen aus Gasen mit Hilfe eines Waschverfahrens durchzuführen, bei dem nicht nur eine praktisch vollständige Reinigung der Gase hinsichtlich dieser Verunreinigungen erreicht wird, sondern auch die Reinigung wegen der Vermeidung von unerwünschten Nebenreaktionen unter höchst wirtschaftlichen Bedingungen erfolgt.The invention has set itself the task of removing the nitrogen compounds from gases with To carry out the help of a washing process in which not only a practically complete cleaning of the Gases in terms of these impurities is achieved, but also the purification because of the avoidance of undesired side reactions takes place under highly economical conditions.
Das erfindungsgemäße Verfahren zum Entfernen von Stickstoffverbindungen (Blausäure, Stickoxyd) aus Gasen durch eine Wäsche des Gases bei im wesentlichen normaler Temperatur, wodurch die Stickstoffverbindungen in der Waschlösung absorbiert und anschließend wieder desorbiert werden, z. B. durch Belüften und/oder Erwärmen der Waschlösung, die anschließend im Kreislauf wieder verwendet wird, ist dabei dadurch gekennzeichnet, daß als Waschlösung eine wäßrige Lösung einer Chelatkomplexyerbindung, die ein ScTiwermetallion aus der IV. Periode des Periodischen Systems jjer Elemente, enthäjt, verwendet "wird." "" " 'Tir111 T ""*" *The inventive method for removing nitrogen compounds (hydrocyanic acid, nitrogen oxide) from gases by washing the gas at essentially normal temperature, whereby the nitrogen compounds are absorbed in the washing solution and then desorbed again, for. B. by venting and / or heating the washing solution, which is then used again in the circuit, is characterized in that ß as a washing solution an aqueous solution of a chelate compound , which is a ScTiwerme tallion from the IV . Period of the Periodic System of each element that contains "is.""""' Tir111 T ""*" *
Unter Chelatkomplexen (s. Römpp »Chemie-Lexikon«,
5. Auflage, 1962) ist ganz allgemein ein mehr oder weniger kompliziert zusammengesetzter
organischer Körper verstanden, der ein oder mehrere Metallionen enthält, welche von mehreren fünf- bis
Verfahren zur Entfernung von
Stickstoffverbindungen aus GasenChelate complexes (see Römpp "Chemie-Lexikon", 5th edition, 1962) are generally understood to mean an organic body with a more or less complex composition, which contains one or more metal ions, which range from several to five to methods for removing
Nitrogen compounds from gases
Anmelder:Applicant:
Heinrich KoppersHeinrich Koppers
Gesellschaft mit beschränkter Haftung,Company with limited liability,
Essen, Moltkestr. 29Essen, Moltkestr. 29
Als Erfinder benannt:
Ortwin Gogolin, MünchenNamed as inventor:
Ortwin Gogolin, Munich
ao sechsgliedrigen Ringen scheren- oder zangenartig umschlossen sind, wobei die in diesen Ringen befindlichen Sauerstoff-, Stickstoff- oder Schwefelatome jeweils Elektronen an das von ihnen umschlossene Metallion abgeben. Die auf diese Weise entstehendeao six-membered rings are enclosed like scissors or pliers, the ones in these rings Oxygen, nitrogen or sulfur atoms each have electrons to the one they enclose Release metal ion. The resulting
as Bindung zwischen Metallion und den erwähnten
Sauerstoff-, Stickstoff- oder Schwefelatomen der Ringe wird im Gegensatz zu der üblichen Valenzbindung
als Koordinationsbindung bezeichnet.
Die Chelatkomplexverbindungen mit dem obenerwähnten allgemeinen Kennzeichen sind außerordentlich
vielfältiger Art und unterscheiden sich voneinander, je nach Art und Anzahl der Ringe und
des koordinativ gebundenen Metallions, durch ihre physikalischen und chemischen Eigenschaften.The bond between the metal ion and the mentioned oxygen, nitrogen or sulfur atoms of the rings is called a coordination bond, in contrast to the usual valence bond.
The chelate complex compounds with the above-mentioned general characteristics are extremely diverse and differ from one another, depending on the type and number of rings and the coordinatively bound metal ion, by their physical and chemical properties.
Die Untersuchungen haben ergeben, daß für die Auswaschung der Stickstoffverbindungen Chelatkomplexverbindungen vorteilhaft sind, die in dem komplexbildenden Anion Carbonsäuregruppen, gegebenenfalls deren Alkali- oder Erdalkalisalze, enthalten, und darunter insbesondere solche Chelatkomplexe, in denen Aminocarbonsäuren bzw. deren Salze vorhanden sind.The investigations have shown that chelate complex compounds are used for leaching the nitrogen compounds The carboxylic acid groups in the complex-forming anion, if appropriate, are advantageous their alkali or alkaline earth salts, including in particular those chelate complexes, in which aminocarboxylic acids or their salts are present.
Ein in der analytischen Chemie wohlbekannter Vertreter dieser Chelatkomplexe, die Aminocarbonsäuren enthalten, geht von der Äthylendiaminotetraessigsäure (EDTA^bzw. deren Alkali- oder Erdalkali- *salzen"äus. Setz? man beispielsweise das Tetranatriumsalz der Äthylendiaminotetraessigsäure mit Eisen_(III)-sulf af um, so bildefsi'cn'eih 'CneTatKbmplex, inA well-known in analytical chemistry representative of this chelate containing amino carboxylic acids, goes from the Äthylendiaminotetra acid (EDTA ^ respectively. Alkali metal or alkaline earth * salt "Aeus. Put? One of Äthylendiami notetraess igsä acid sen_ example, the tetrasodium salt with egg ( III) -sulf af um, so bildefsi'cn'eih 'CneTatKbmplex, in
welcHem ein baer mehrere Eisenionen teilweise durch echte Valenzbindungen und zusätzlich durch koordinative Bindungen gebunden werden. Die wäßrigewhat a baer partially through several iron ions real valence bonds and additionally bound by coordinative bonds. The watery one
709677/335709677/335
Lösung des EDTA-Eisen(lll)-Chelates ist tiefrot, die des EDTA-Eisen(lI)-Chelates gelb gefärbt.Solution of the EDTA iron (lll) chelate is deep red, the of the EDTA iron (lI) chelate colored yellow.
Andere Vertreter dieser Klasse sind u. a. die Hydroxyäthyldiaminoäthylentriessigsäure, Diäthylentriaminpentaessigsäure, Äthylendiamindi(O-hydroxyphenyl)essigsäure, Diaminoäthyläthertetraessigsäure, Äthylen glycol - bis (aminoäthyl äther) - tetra essigsäure, l^-DiaminocyclohexantetraessigsäurejUramildiessigsäure, Hydroxyäthylnitrilodiessigsäure, Anilindiessigsäure und deren ein-, zwei- oder mehrbasische Alkalioder Erdalkalisalze und andere Aminocarbonsalze.Other representatives of this class include: Hydroxyäthyldiaminoäthylenetriacetic acid, Diethylenetriaminepentaacetic acid, ethylenediaminedi (O-hydroxyphenyl) acetic acid, Diaminoethyl ether tetraacetic acid, ethylene glycol - bis (aminoethyl ether) - tetra acetic acid, l ^ -diaminocyclohexanetetraacetic acid, uramildiacetic acid, Hydroxyäthylnitrilodiacetic acid, anilinediacetic acid and their mono-, di- or polybasic alkali or Alkaline earth salts and other aminocarboxylic salts.
Neben den schon erwähnten Carbonsäuren und Aminocarbonsäuren können aber auch andere organische Gruppen, vor allem stickstoffhaltige Komplexe als chelatkomplexbildende Anionen angewandt werden.In addition to the carboxylic acids and aminocarboxylic acids already mentioned, other organic Groups, especially nitrogen-containing complexes, used as chelate complex-forming anions will.
Als Beispiele hierfür seien genannt: Äthylendiamin, Diäthylentriamin, Triäthylentetramin, Tetraäthylenpentamin und höhere Polyäthylenamine; ferner 1,2-Diamine, wie Propylendiamin, Dipropylentriamin usw., und 1,2-, 3,4-Tetramine, wie Butadientetramine usw.Examples include: ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylene pentamine and higher polyethylene amines; also 1,2-diamines, such as propylenediamine and dipropylenetriamine etc., and 1,2-, 3,4-tetramines such as butadiene tetramines etc.
Für die Auswahl des für einen konkreten Anwendungsfall zweckmäßigsten»Chelatkomplexes ist auch noch der Gesichtspunkt wesentlich, daß die hauptsächlichen Bestandteile des zu reinigenden Gases, wie Wasserstoff, Kohlenoxyd, Kohlendioxyd, Aromaten, gesättigte und ungesättigte Aliphate usw., keinen nachteiligen Einfluß auf die Stabilität des Chelatkomplexes ausüben. Es wurde in diesem Zusammenhang gefunden, daß Chelatkomplexe mit großer Wasserlöslichkeit, das sind insbesondere solche mit mindestens zwei Carbonsäuregruppen je Komplex, von den Hauptbestandteilen der üblichen technischen Gase praktisch nicht beeinflußt werden.For the selection of the most appropriate »chelate complex for a specific application, nor the point of view essential that the main components of the gas to be purified, such as Hydrogen, carbon dioxide, carbon dioxide, aromatics, saturated and unsaturated aliphatics, etc., none exert a detrimental effect on the stability of the chelate complex. It was in this context found that chelate complexes with high water solubility, especially those with at least two carboxylic acid groups per complex, from the main components of the usual technical Gases are practically not influenced.
Die Waschlösung hat zweckmäßigerweise einen pH-Wert zwischen 6 und 8. Stärker alkalische Lösungen können jedoch oft bessere Ergebnisse erzielen.The washing solution expediently has a pH value between 6 and 8. More alkaline solutions however, can often achieve better results.
Die Regenerierung der Waschlösung erfolgt am einfachsten durch Belüftung. Die Belüftung bewirkt gleichzeitig eine Reoxydation des Chelatkomplexes und eine Austreibung der Stickstoffverbindungen. Das Stickoxyd wird dabei, falls die Waschlösung durch irgendwelche Umstände in reduzierter Form vorliegt, zum Teil bis zum Stickstoff, gegebenenfalls bis zum Ammoniak reduziert. Die Blausäure wird im allgemeinen nicht verändert. Es entweicht also Blausäure mit der Belüftungsluft. Eine Erwärmung der Waschlösung auf Temperaturen unter 100° C genügt in den meisten Fällen ebenfalls zur Regenerierung.The easiest way to regenerate the washing solution is to use aeration. The ventilation causes at the same time reoxidation of the chelate complex and expulsion of nitrogen compounds. The nitric oxide is in this case, if the washing solution by any circumstances in a reduced form is present, partly reduced to nitrogen, optionally reduced to ammonia. The hydrocyanic acid is in the general not changed. So hydrogen cyanide escapes with the ventilation air. A warming of the Washing solution at temperatures below 100 ° C is also sufficient for regeneration in most cases.
Ein entschwefeltes Koksofengas enthielt 60 g Blausäure je 100 Nm3. Das Gas wurde bei einer Temperatur von 25° C mit einer wäßrigen Lösung von Fe2(III)Na0(EDTA)3 in einer Menge von 1,5 m8 Lösung je 1000 Nm3 Gas gewaschen. Die Konzentration der Lösung betrug 0,2 Mol Chelatkomplex je Liter. Nach der Waschung betrug der Blausäuregehalt des Gases noch etwa 1 g je 100 Nm3. Der Auswaschungsgrad betrug demnach 98,5%.A desulfurized coke oven gas contained 60 g hydrogen cyanide per 100 Nm 3 . The gas was washed at a temperature of 25 ° C. with an aqueous solution of Fe 2 (III) Na 0 (EDTA) 3 in an amount of 1.5 m 8 of solution per 1000 Nm 3 of gas. The concentration of the solution was 0.2 mol of chelate complex per liter. After washing, the hydrogen cyanide content of the gas was still about 1 g per 100 Nm 3 . The degree of leaching was accordingly 98.5%.
Tn einem anderen Fall wurde ein Restgas aus einem chemischen Prozeß behandelt, dessen Blausäuregehalt 330 g je 100Nm3 betrug. Die Waschung erfolgte unter sonst gleichen Bedingungen. Es konnte ein Auswaschungsgrad von 77,9% erreicht werden.In another case, a residual gas from a chemical process was treated, the hydrogen cyanide content of which was 330 g per 100 Nm 3 . The washing took place under otherwise identical conditions. A degree of leaching of 77.9% could be achieved.
Ein weitgehend gereinigtes Koksofengas enthieltContained a largely purified coke oven gas
Stickoxyd in einer Menge von ] 2 Kubikzentimeter je Nm3 Gas. Unter den schon vorstehend beschriebenenNitrogen oxide in an amount of] 2 cubic centimeters per Nm 3 gas. Among those already described above
ao Bedingungen erfolgt eine Wäsche des Gases mit Chelatlösung. Der Stickstoffgehalt des Gases ging auf etwa 0,6 Kubikzentimeter je Nms Gas zurück. Der Auswaschungsgrad betrug demnach etwa 95%.Under certain conditions, the gas is scrubbed with chelate solution. The nitrogen content of the gas decreased to about 0.6 cubic centimeters per Nm s of gas. The degree of leaching was accordingly about 95%.
Wurde die Chelatlösung durch die gleichzeitige Anwesenheit von Schwefelwasserstoff reduziert, so erhöhte sich der Auswaschungsgrad des Stickoxyds auf 98 bis 99%.If the chelate solution was reduced by the simultaneous presence of hydrogen sulfide, so the degree of leaching of nitrogen oxide increased to 98 to 99%.
Claims (2)
Französische Patentschrift Nr. 1302767.Considered publications:
French patent specification No. 1302767.
Publications (1)
Publication Number | Publication Date |
---|---|
DE1251900B true DE1251900B (en) | 1967-10-12 |
Family
ID=605072
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DENDAT1251900D Pending DE1251900B (en) | Process for removing nitrogen compounds from gases |
Country Status (1)
Country | Link |
---|---|
DE (1) | DE1251900B (en) |
Cited By (22)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4964561A (en) * | 1972-10-25 | 1974-06-22 | ||
DE2416660A1 (en) * | 1973-04-09 | 1974-10-24 | Mitsui Petrochemical Ind | PROCEDURE FOR THE REMOVAL OF NITROGEN OXYDE FROM A GAS |
DE2445567A1 (en) * | 1973-09-24 | 1975-04-03 | Asahi Chemical Ind | PROCEDURE FOR REMOVING NITROGEN MONOXIDE FROM A GAS CONTAINING NITROGEN MONOXIDE |
US3991161A (en) * | 1974-01-21 | 1976-11-09 | Kureha Kagaku Kogyo Kabushiki Kaisha | Method of removing nitrogen oxides from a gas and for converting same to ammonium sulfate |
US4013430A (en) * | 1974-12-28 | 1977-03-22 | Chisso Corporation | Process for regenerating absorbing solution used for exhaust gas purification |
JPS5213504B2 (en) * | 1973-04-25 | 1977-04-14 | ||
JPS5213788B2 (en) * | 1974-05-02 | 1977-04-16 | ||
US4035470A (en) * | 1974-11-02 | 1977-07-12 | Fuji Kasui Engineering Co., Ltd. | Process for removing sulfur oxides and/or nitrogen oxides from waste gas |
JPS5228109B2 (en) * | 1973-04-25 | 1977-07-25 | ||
US4044101A (en) * | 1974-12-21 | 1977-08-23 | Asahi Kasei Kogyo Kabushiki Kaisha | Method of treating exhaust gases containing nitrogen oxides and sulfurous acid gas |
US4079118A (en) * | 1973-12-27 | 1978-03-14 | Chisso Engineering Co Ltd | Method for removing nitrogen oxides using ferricion-EDTA complex solutions |
US4081509A (en) * | 1975-03-31 | 1978-03-28 | Hitachi, Ltd. | Method for removing nitrogen oxides from flue gas by absorption |
US4087372A (en) * | 1973-10-31 | 1978-05-02 | Kureha Kagaku Kogyo Kabushiki Kaisha | An absorbing solution for the removal of nitrogen oxide form a gas containing same |
US4091074A (en) * | 1976-01-27 | 1978-05-23 | Chisso Engineering Co Ltd. | Method for regenerating iron-EDTA solutions used for scrubbing plug gases |
JPS5333955B2 (en) * | 1973-09-21 | 1978-09-18 | ||
US4158044A (en) * | 1973-04-09 | 1979-06-12 | Mitsui Shipbuilding And Engineering Co. | Method for removing nitric oxide from industrial gases |
FR2451213A1 (en) * | 1979-03-13 | 1980-10-10 | Inst Francais Du Petrole | Nitric oxide removal from gases - by absorption in mixt. of di:alkyl-amide and ferrous salt |
FR2452957A1 (en) * | 1979-04-06 | 1980-10-31 | Inst Francais Du Petrole | Sepg. hydrogen sulphide and nitrogen oxide simultaneously - from gas mixts., using chelated iron salt with iron at least, partly ter-valent |
DE3514407A1 (en) * | 1985-04-20 | 1986-10-23 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Multiple-stage HCl-, SO2- and NOx- scrubbing process for flue gas purification, preferably downstream of fossil-fuel power stations, having high sodium sulphite contents in the SO2- and NOx scrubbing stage and corresponding water treatment |
DE3517483A1 (en) * | 1985-05-15 | 1986-11-20 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Process for the simultaneous scrubbing of SO2 and NOx by a high sodium-sulphate content with simultaneously high residence time in the scrubber |
DE3523354A1 (en) * | 1985-06-29 | 1987-01-08 | Hoelter Heinz | Simultaneous SO2 and NOx scrubbing downstream of combustion plants with simultaneous stabilization of the iron salt complexes in the scrubbing solution |
EP0243889A1 (en) * | 1986-04-24 | 1987-11-04 | Europäische Atomgemeinschaft (Euratom) | Process and apparatus for denitrifying waste gases |
-
0
- DE DENDAT1251900D patent/DE1251900B/en active Pending
Cited By (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4964561A (en) * | 1972-10-25 | 1974-06-22 | ||
JPS5210659B2 (en) * | 1973-04-09 | 1977-03-25 | ||
DE2416660A1 (en) * | 1973-04-09 | 1974-10-24 | Mitsui Petrochemical Ind | PROCEDURE FOR THE REMOVAL OF NITROGEN OXYDE FROM A GAS |
US4158044A (en) * | 1973-04-09 | 1979-06-12 | Mitsui Shipbuilding And Engineering Co. | Method for removing nitric oxide from industrial gases |
JPS5228109B2 (en) * | 1973-04-25 | 1977-07-25 | ||
JPS5213504B2 (en) * | 1973-04-25 | 1977-04-14 | ||
JPS5333955B2 (en) * | 1973-09-21 | 1978-09-18 | ||
US3984522A (en) * | 1973-09-24 | 1976-10-05 | Asahi Kasei Kogyo Kabushiki Kaisha | Method of removing nitrogen monoxide from a nitrogen monoxide-containing gas |
DE2445567A1 (en) * | 1973-09-24 | 1975-04-03 | Asahi Chemical Ind | PROCEDURE FOR REMOVING NITROGEN MONOXIDE FROM A GAS CONTAINING NITROGEN MONOXIDE |
US4087372A (en) * | 1973-10-31 | 1978-05-02 | Kureha Kagaku Kogyo Kabushiki Kaisha | An absorbing solution for the removal of nitrogen oxide form a gas containing same |
US4079118A (en) * | 1973-12-27 | 1978-03-14 | Chisso Engineering Co Ltd | Method for removing nitrogen oxides using ferricion-EDTA complex solutions |
US3992508A (en) * | 1974-01-21 | 1976-11-16 | Kureha Kagaku Kogyo Kabushiki Kaisha | Method of removing nitrogen oxides from a gas containing nitrogen oxides |
US3991161A (en) * | 1974-01-21 | 1976-11-09 | Kureha Kagaku Kogyo Kabushiki Kaisha | Method of removing nitrogen oxides from a gas and for converting same to ammonium sulfate |
JPS5213788B2 (en) * | 1974-05-02 | 1977-04-16 | ||
US4035470A (en) * | 1974-11-02 | 1977-07-12 | Fuji Kasui Engineering Co., Ltd. | Process for removing sulfur oxides and/or nitrogen oxides from waste gas |
US4044101A (en) * | 1974-12-21 | 1977-08-23 | Asahi Kasei Kogyo Kabushiki Kaisha | Method of treating exhaust gases containing nitrogen oxides and sulfurous acid gas |
US4013430A (en) * | 1974-12-28 | 1977-03-22 | Chisso Corporation | Process for regenerating absorbing solution used for exhaust gas purification |
US4081509A (en) * | 1975-03-31 | 1978-03-28 | Hitachi, Ltd. | Method for removing nitrogen oxides from flue gas by absorption |
US4091074A (en) * | 1976-01-27 | 1978-05-23 | Chisso Engineering Co Ltd. | Method for regenerating iron-EDTA solutions used for scrubbing plug gases |
FR2451213A1 (en) * | 1979-03-13 | 1980-10-10 | Inst Francais Du Petrole | Nitric oxide removal from gases - by absorption in mixt. of di:alkyl-amide and ferrous salt |
FR2452957A1 (en) * | 1979-04-06 | 1980-10-31 | Inst Francais Du Petrole | Sepg. hydrogen sulphide and nitrogen oxide simultaneously - from gas mixts., using chelated iron salt with iron at least, partly ter-valent |
DE3514407A1 (en) * | 1985-04-20 | 1986-10-23 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Multiple-stage HCl-, SO2- and NOx- scrubbing process for flue gas purification, preferably downstream of fossil-fuel power stations, having high sodium sulphite contents in the SO2- and NOx scrubbing stage and corresponding water treatment |
DE3517483A1 (en) * | 1985-05-15 | 1986-11-20 | Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck | Process for the simultaneous scrubbing of SO2 and NOx by a high sodium-sulphate content with simultaneously high residence time in the scrubber |
DE3523354A1 (en) * | 1985-06-29 | 1987-01-08 | Hoelter Heinz | Simultaneous SO2 and NOx scrubbing downstream of combustion plants with simultaneous stabilization of the iron salt complexes in the scrubbing solution |
EP0243889A1 (en) * | 1986-04-24 | 1987-11-04 | Europäische Atomgemeinschaft (Euratom) | Process and apparatus for denitrifying waste gases |
WO1987006493A1 (en) * | 1986-04-24 | 1987-11-05 | Europäische Atomgemeinschaft (Euratom) | Process and device for removing nitrogen from flue gases |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE1251900B (en) | Process for removing nitrogen compounds from gases | |
DE2755569C2 (en) | ||
DE875847C (en) | Process for cleaning gases, in particular coke oven gases, from sulfur compounds | |
DE2423828B2 (en) | Process for cleaning industrial gases | |
DE2946193A1 (en) | METHOD AND ABSORPTION SOLUTION FOR REMOVING CARBON DIOXIDE AND / OR HYDROGEN SULFUR FROM GAS MIXTURES | |
DE1000356B (en) | Process for the separation and recovery of carbonic acid from gas mixtures | |
DE1253686B (en) | Process for removing nitrogen oxides from industrial exhaust gases | |
DE2246090A1 (en) | PROCESS FOR THE REGENERATION OF STRONG BASES ON THE BASIS OF SOLUTIONS OF THEIR SULPHIDES WITH THE SIMULTANEOUS RECOVERY OF SULFUR | |
DE1064479B (en) | Process for removing hydrogen sulfide from gas mixtures, such as coke oven gas | |
DE620932C (en) | Process for removing weak gaseous acids from gases | |
DE743088C (en) | Process for the selective scrubbing of hydrogen sulfide from gases containing carbon dioxide, in particular distillation gases by means of acid-free ammonia water | |
DE1233836B (en) | Process for the production of ammonia gas | |
DE4201920A1 (en) | METHOD FOR REMOVING ACID GASES FROM GAS MIXTURES | |
DE3706619A1 (en) | METHOD FOR REMOVING SULFURIZING GASES | |
DE2230594A1 (en) | METHOD FOR REMOVING HEAVY METAL IONS FROM A SOLUTION | |
DE812909C (en) | Process for the production of urea | |
DE1544006A1 (en) | Process for corrosion inhibition in gas scrubbing processes | |
DE702605C (en) | Process for removing organically bound sulfur from water gas | |
DE3821350A1 (en) | SELECTIVE SEPARATION OF RHODANIDE IONS FROM A DETERGENT | |
DE542343C (en) | Process for purifying water and sewage | |
DE1667648C (en) | Method to reduce the formation of lumps in ammonium nitrate | |
DE3620073C1 (en) | Regenerative process for exhaust gas purification | |
DE216463C (en) | ||
DE700553C (en) | Process for the separation of ammonia and carbon dioxide | |
DE1150962B (en) | Process for the separation of tungsten compounds from aqueous, tungsten-containing solutions |