DE1281400B - Process for the continuous separation of gases according to the principle of gas elution chromatography - Google Patents
Process for the continuous separation of gases according to the principle of gas elution chromatographyInfo
- Publication number
- DE1281400B DE1281400B DEP20395A DEP0020395A DE1281400B DE 1281400 B DE1281400 B DE 1281400B DE P20395 A DEP20395 A DE P20395A DE P0020395 A DEP0020395 A DE P0020395A DE 1281400 B DE1281400 B DE 1281400B
- Authority
- DE
- Germany
- Prior art keywords
- gas
- principle
- separated
- continuous separation
- elution chromatography
- 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 23
- 238000000926 separation method Methods 0.000 title claims description 11
- 238000000034 method Methods 0.000 title claims description 10
- 238000004587 chromatography analysis Methods 0.000 title claims description 5
- 238000010828 elution Methods 0.000 title claims description 5
- 239000000463 material Substances 0.000 claims description 10
- 239000000203 mixture Substances 0.000 claims description 9
- 239000012159 carrier gas Substances 0.000 claims description 8
- 230000005012 migration Effects 0.000 claims description 6
- 238000013508 migration Methods 0.000 claims description 6
- 239000003245 coal Substances 0.000 claims 1
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 4
- 239000007791 liquid phase Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 4
- 239000012876 carrier material Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 238000004810 partition chromatography Methods 0.000 description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N sec-butylidene Natural products CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 2
- IAQRGUVFOMOMEM-ONEGZZNKSA-N trans-but-2-ene Chemical compound C\C=C\C IAQRGUVFOMOMEM-ONEGZZNKSA-N 0.000 description 2
- 239000011149 active material Substances 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002996 emotional effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
- G01N30/02—Column chromatography
- G01N30/50—Conditioning of the sorbent material or stationary liquid
- G01N30/58—Conditioning of the sorbent material or stationary liquid the sorbent moving as a whole
-
- H—ELECTRICITY
- H04—ELECTRIC COMMUNICATION TECHNIQUE
- H04L—TRANSMISSION OF DIGITAL INFORMATION, e.g. TELEGRAPHIC COMMUNICATION
- H04L25/00—Baseband systems
- H04L25/02—Details ; arrangements for supplying electrical power along data transmission lines
- H04L25/20—Repeater circuits; Relay circuits
- H04L25/24—Relay circuits using discharge tubes or semiconductor devices
Landscapes
- Engineering & Computer Science (AREA)
- Immunology (AREA)
- Health & Medical Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- Power Engineering (AREA)
- Pathology (AREA)
- Computer Networks & Wireless Communication (AREA)
- Signal Processing (AREA)
- Dc-Dc Converters (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Ignition Installations For Internal Combustion Engines (AREA)
Description
DEUTSCHESGERMAN
PATENTAMTPATENT OFFICE
Int. Cl.:Int. Cl .:
Nummer:
Aktenzeichen:
Anmeldetag:
Auslegetag:Number:
File number:
Registration date:
Display day:
BOIdBOId
B 01 j; A 62 c
GOIn B 01 j; A 62 c
GOIn
12 e - 3/02 12 e - 3/02
12 g-1/0112 g-1/01
421-4/16421-4 / 16
P 12 81 400.5-43 (P 20395)P 12 81 400.5-43 (P 20395)
26. März 1958March 26, 1958
31. Oktober 1968October 31, 1968
Bekanntlich zeichnet sich die Elutions-Chromatographie durch besondere Eignung zur Trennung chemisch sehr ähnlicher Verbindungen aus. Die Trennwirkung ist um Größenordnungen besser als bei Rektifikationsmethoden; außerdem gestattet die Gas-Lösungs-Verteilungs-Chromatographie durch zweckmäßige Wahl der stationären flüssigen Phase eine Anpassung an spezielle Trennungsprobleme, die es z. B. ermöglicht, Paraffine und Olefine gleichen Siedepunktes voneinander zu trennen. Die Methode konnte bisher nur diskontinuierlich durchgeführt werden und blieb auf analytische Trennungen beschränkt. As is well known, elution chromatography is known due to its particular suitability for separating chemically very similar compounds. the The separation effect is orders of magnitude better than with rectification methods; also allows the Gas-solution partition chromatography through appropriate choice of the stationary liquid phase an adaptation to special separation problems, which are z. B. enables paraffins and olefins to be the same Separate boiling point from each other. So far, the method could only be carried out discontinuously become and remained limited to analytical separations.
Überraschenderweise wurde gefunden, daß es möglich ist, das Prinzip der Elutions-Chromatographie für ein kontinuierliches Verfahren zur Trennung von Gasen zu verwenden, indem ein chromatographisch aktives Material —■ beispielsweise Di-n-butyl-phthalat auf Schamottemehl (Sterchamol 0,3 bis 0,4 mm Körnung), 40/100 Gewichtsanteile — im folgenden kurz Material genannt, und eine Gasphase in einer Säule im Gegenstrom zueinander mit definierter Geschwindigkeit bewegt werden. Die Gasphase besteht aus zu trennendem Gemisch, das mit Trägergas verdünnt ist. Alle Gaskomponenten bewegen sich im Gegenstrom zum Material, aber jede Komponente mit der ihr stoffeigenen, durch Verteilungs- bzw. Adsorptionsisothermen bestimmten Geschwindigkeit.It has surprisingly been found that it is possible to use the principle of elution chromatography to use for a continuous process for the separation of gases by a chromatograph active material - ■ for example di-n-butyl phthalate on fireclay flour (sterchamol 0.3 to 0.4 mm grain size), 40/100 parts by weight - hereinafter referred to as material for short, and one Gas phase are moved in a column in countercurrent to each other at a defined speed. the The gas phase consists of the mixture to be separated, which is diluted with carrier gas. All gas components move in countercurrent to the material, but through each component with its own material Distribution or adsorption isotherms determined speed.
Es wurde gefunden, daß die Geschwindigkeit des Materials und die Strömungsgeschwindigkeit der Gasphase so aufeinander abgestimmt werden müssen, daß von zwei zu trennenden Komponenten die eine schneller und die andere langsamer wandert, als sich das Material in entgegengesetzter Richtung bewegt. In diesem Fall strömt das Gas mit der größeren Wanderungsgeschwindigkeit quantitativ mit dem Trägergas zum Kopf der Säule, während das Gas mit der geringeren Wanderungsgeschwindigkeit quantitativ zum Fuß der Säule transportiert wird, wo es in einer zweiten Stufe vom Material abgelöst werden muß, ζ. B. durch einen Trägergasstrom bei größerer Gasphasengeschwindigkeit.It has been found that the speed of the material and the flow rate of the Gas phase must be coordinated so that the two components to be separated one moves faster and the other slower than the material moves in the opposite direction emotional. In this case, the gas flows quantitatively with the greater migration speed the carrier gas to the top of the column, while the gas with the lower migration speed is quantitatively transported to the base of the column, where it is detached from the material in a second stage must be, ζ. B. by a carrier gas flow at a higher gas phase velocity.
Besonders geeignet für die kontinuierliche Trennung von zwei Gasen ist die Einstellung der Materialgeschwindigkeit
auf den Mittelwert der Wanderungsgeschwindigkeiten dieser beiden Gase. Die voneinander
getrennten Komponenten fallen im Gemisch mit Trägergas an, das darum so auszuwählen ist,
daß die Abtrennung der eluierten Verbindungen vom Trägergas nach bekannten Methoden durchgeführt
werden kann. Als Trägergas können Wasserstoff, Verfahren zur kontinuierlichen Trennung von
Gasen nach dem Prinzip der
Gas-Elutions-ChromatographieSetting the material speed to the mean value of the migration speeds of these two gases is particularly suitable for the continuous separation of two gases. The components separated from one another are obtained in a mixture with carrier gas, which is therefore to be selected so that the eluted compounds can be separated from the carrier gas by known methods. Hydrogen, a process for the continuous separation of
Gases according to the principle of
Gas elution chromatography
Anmelder:Applicant:
Dr. phil. Helmut Pichler,Dr. phil. Helmut Pichler,
7500 Karlsruhe, Kaiserstr. 127500 Karlsruhe, Kaiserstr. 12th
Als Erfinder benannt:Named as inventor:
Dr. phil. Helmut Pichler,Dr. phil. Helmut Pichler,
Dr. Hans Schulz, 7500 KarlsruheDr. Hans Schulz, 7500 Karlsruhe
Helium, Stickstoff, Luft, Kohlendioxyd u. a. verwendet werden. Das Material ist nach dem Ausspülen der langsamer wandernden Verbindungen regeneriert und wird im Kreislauf geführt.Helium, nitrogen, air, carbon dioxide and others. be used. The material is after rinsing the slower moving compounds are regenerated and circulated.
Das Verfahren ist anwendbar auf die Trennung von zwei Gasen voneinander bzw. auf die Abtrennung der Komponente mit der kleinsten oder der größten Wanderungsgeschwindigkeit aus einem Vielstoffgemisch bzw. auf die Zerlegung eines Mehrstoffgemisches in zwei Fraktionen, in denen die einzelnen Komponenten nur noch in einer der beiden Fraktionen enthalten sind. Die wiederholte Anwendung des Prinzips gestattet es, alle Komponenten des Gemisches voneinander zu trennen. Temperatur und Druck müssen so eingehalten werden, daß die zu trennenden Verbindungen gasförmig vorliegen. Als inertes Trägermaterial und als flüssige Phase werden von der Verteilungschromatographie her bekannte Stoffe verwendet. Das Verfahren dient besonders zur kontinuierlichen Trennung von Gasen, die nach bisher bekannten Methoden nur schwer oder überhaupt nicht voneinander getrennt werden können.The method is applicable to the separation of two gases from one another or to the separation the component with the lowest or the highest migration speed from a multicomponent mixture or the breakdown of a multi-component mixture into two fractions, in which the individual Components are now only contained in one of the two fractions. Repeated application the principle allows all components of the mixture to be separated from one another. Temperature and Pressure must be maintained in such a way that the compounds to be separated are in gaseous form. as inert carrier material and the liquid phase are known from partition chromatography Fabrics used. The method is used particularly for the continuous separation of gases, which after so far known methods can only be separated from one another with difficulty or not at all.
AusführungsbeispielEmbodiment
Aufzutrennendes Gemisch:Mixture to be separated:
η-Butan (Sdp. -0,50C) 50 Volumprozent,
trans-Buten (Sdp. +0,90C) 50 Volumprozent;η-butane (bp. -0.5 0 C) 50 volume percent,
trans-butene (. b.p. +0.9 0 C) 50 volume percent;
Trägergas: Stickstoff;Carrier gas: nitrogen;
Inertes Trägermaterial: Schamottemehl (Sterchamol), Körnung 0,3 bis 0,4 mm;Inert carrier material: fireclay powder (Sterchamol), grain size 0.3 to 0.4 mm;
Flüssige Phase: Di-n-butyl-phthalat;Liquid phase: di-n-butyl phthalate;
Gramm flüssige Phase pro Gramm Trägermaterial: 40/100;Grams of liquid phase per gram of carrier material: 40/100;
Materialgeschwindigkeit: 12 cm/min;Material speed: 12 cm / min;
Strömung: 42 cm3 pro Minute und pro cm2 Säulenquerschnitt; Flow: 42 cm 3 per minute and per cm 2 of column cross-section;
809 629/1429809 629/1429
Volumen aufgegebenes Gemisch pro Volumen Trägergas: 0,2.Volume of mixture applied per volume of carrier gas: 0.2.
Die Analysen von Gasproben zeigen, daß n-Butan und trans-Buten unter diesen Bedingungen voneinander kontinuierlich quantitativ getrennt werden.Analyzes of gas samples show that n-butane and trans-butene are different from each other under these conditions continuously quantitatively separated.
Claims (2)
Bd. 1, 1951, S. 356 und 357;Uli mann, Encyclopedia of Techn. Chemistry,
Vol. 1, 1951, pp. 356 and 357;
bis 597;Journal "Erdöl u. Coal", 9 (1956), p. 593
to 597;
S. 1056.VDI-Zeitschrift, 98, 1956, No. 20 (July 11th),
P. 1056.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP20395A DE1281400B (en) | 1958-03-26 | 1958-03-26 | Process for the continuous separation of gases according to the principle of gas elution chromatography |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP20395A DE1281400B (en) | 1958-03-26 | 1958-03-26 | Process for the continuous separation of gases according to the principle of gas elution chromatography |
| DES96883A DE1281480B (en) | 1965-04-30 | 1965-04-30 | Circuit arrangement for alternately connecting the poles of a voltage source to a consumer, in particular a single-current-double-current telegraph converter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| DE1281400B true DE1281400B (en) | 1968-10-24 |
Family
ID=7520351
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DEP20395A Pending DE1281400B (en) | 1958-03-26 | 1958-03-26 | Process for the continuous separation of gases according to the principle of gas elution chromatography |
| DES96883A Pending DE1281480B (en) | 1958-03-26 | 1965-04-30 | Circuit arrangement for alternately connecting the poles of a voltage source to a consumer, in particular a single-current-double-current telegraph converter |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| DES96883A Pending DE1281480B (en) | 1958-03-26 | 1965-04-30 | Circuit arrangement for alternately connecting the poles of a voltage source to a consumer, in particular a single-current-double-current telegraph converter |
Country Status (6)
| Country | Link |
|---|---|
| BE (1) | BE680338A (en) |
| DE (2) | DE1281400B (en) |
| FR (1) | FR1472514A (en) |
| GB (1) | GB1140059A (en) |
| NL (1) | NL6605732A (en) |
| SE (1) | SE328018B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT1209311B (en) * | 1980-02-29 | 1989-07-16 | Sits Soc It Telecom Siemens | TONE GENERATOR FOR TIME DIVISION TELEPHONE UNITS. |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2635706A (en) * | 1949-08-29 | 1953-04-21 | Phillips Petroleum Co | Selective adsorption separation apparatus |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1036906B (en) * | 1956-06-15 | 1958-08-21 | Siemens Ag | Relayless circuit arrangement for generating current signals for telex purposes |
| BE558426A (en) * | 1956-06-15 | |||
| NL249099A (en) * | 1957-02-01 |
-
1958
- 1958-03-26 DE DEP20395A patent/DE1281400B/en active Pending
-
1965
- 1965-04-30 DE DES96883A patent/DE1281480B/en active Pending
-
1966
- 1966-03-23 FR FR54691A patent/FR1472514A/en not_active Expired
- 1966-04-28 NL NL6605732A patent/NL6605732A/xx unknown
- 1966-04-29 SE SE05866/68A patent/SE328018B/xx unknown
- 1966-04-29 BE BE680338D patent/BE680338A/xx unknown
- 1966-05-02 GB GB19160/66A patent/GB1140059A/en not_active Expired
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2635706A (en) * | 1949-08-29 | 1953-04-21 | Phillips Petroleum Co | Selective adsorption separation apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| GB1140059A (en) | 1969-01-15 |
| NL6605732A (en) | 1966-10-31 |
| FR1472514A (en) | 1967-03-10 |
| BE680338A (en) | 1966-10-31 |
| DE1281480B (en) | 1968-10-31 |
| SE328018B (en) | 1970-09-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| DE2218799C2 (en) | Method and device for obtaining a light gas from a gas mixture | |
| DE1281400B (en) | Process for the continuous separation of gases according to the principle of gas elution chromatography | |
| DE3740313A1 (en) | METHOD FOR SEPARATING 2,6-DIMETHYLNAPHTHALINE | |
| DE1114475B (en) | Continuous process for the recovery of pure, gaseous, unsaturated hydrocarbons from an at least internal gas mixture by means of extraction with solvents | |
| DE2918172C2 (en) | ||
| DE2361654A1 (en) | PROCESS FOR SEPARATING AETHYLBENZENE FROM A MIXTURE OF C LOW 8 FLAVORS AND FAUJASITE SUITABLE FOR CARRYING OUT THIS PROCESS | |
| DE871886C (en) | Adsorption process | |
| GB1480439A (en) | Method for the finish machining of components of apparatus for use in the separation of gaseous or vapour substances of different molecular weights | |
| US3223747A (en) | Continuous fixed bed vapor-liquid partition chromatograph | |
| DE2626893A1 (en) | METHOD AND DEVICE FOR ADSORPTION OF GAS | |
| DE1064479B (en) | Process for removing hydrogen sulfide from gas mixtures, such as coke oven gas | |
| DE69116615T2 (en) | METHOD OF DESULFURING A GAS MIXTURE CONTAINING H2S AND SO2 WITH RECOVERY OF THESE COMPOUNDS IN THE FORM OF SULFUR | |
| DE2630915C3 (en) | Process for the separation of ethylbenzene from xylene isomer mixtures | |
| DE1036223B (en) | Process for the recovery of water enriched in heavy water in the course of ammonia synthesis using an isotope exchange between ammonia and hydrogen gas | |
| DE2612064C2 (en) | ||
| DE399953C (en) | Process for the extraction of components from gas or vapor mixtures by means of adsorption | |
| DE1568172C (en) | Process for separating one or more hydrocarbons from mixtures of alkyl aromatic and / or alkenyl aromatic hydrocarbons | |
| DE2000206C3 (en) | Molecular Sieve Separation Process | |
| DE369107C (en) | Process for separating and recovering gases and vapors from mixtures | |
| DE1931414B2 (en) | METHOD AND DEVICE FOR CLEANING HEAVY WATER | |
| DE1119825B (en) | Method and device for the separation of mixtures of substances | |
| DE972047C (en) | Process for the separation of mixtures of solid particles of different porosity | |
| DE816873C (en) | Process for the desulphurization of gases | |
| DE1254134B (en) | Process for the enrichment of deuterium with respect to its isotopes according to the bit temperature exchange method | |
| DE1419686A1 (en) | Continuous gas chromatic process and device for its implementation |