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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 chromatography

Info

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
Application number
DEP20395A
Other languages
German (de)
Inventor
Dr Phil Helmut Pichler
Dr Hans Schulz
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
PHIL HELMUT PICHLER DR
Original Assignee
PHIL HELMUT PICHLER DR
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by PHIL HELMUT PICHLER DR filed Critical PHIL HELMUT PICHLER DR
Priority to DEP20395A priority Critical patent/DE1281400B/en
Publication of DE1281400B publication Critical patent/DE1281400B/en
Pending legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02Column chromatography
    • G01N30/50Conditioning of the sorbent material or stationary liquid
    • G01N30/58Conditioning of the sorbent material or stationary liquid the sorbent moving as a whole
    • HELECTRICITY
    • H04ELECTRIC COMMUNICATION TECHNIQUE
    • H04LTRANSMISSION OF DIGITAL INFORMATION, e.g. TELEGRAPHIC COMMUNICATION
    • H04L25/00Baseband systems
    • H04L25/02Details ; arrangements for supplying electrical power along data transmission lines
    • H04L25/20Repeater circuits; Relay circuits
    • H04L25/24Relay circuits using discharge tubes or semiconductor devices

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  • 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

BUNDESREPUBLIK DEUTSCHLANDFEDERAL REPUBLIC OF GERMANY

DEUTSCHESGERMAN

PATENTAMTPATENT OFFICE

AUSLEGESCHRIFTEDITORIAL

Int. Cl.:Int. Cl .:

Deutsche Kl.:German class:

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-Chromatographie
Setting 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)

Patentansprüche:Patent claims: 1. Verfahren zur kontinuierlichen Trennung von ein Trägergas enthaltenden Gasgemischen nach dem Prinzip der Gas-Elutions-Chromatographie, dadurch gekennzeichnet, daß Säulenmaterial mit einer Geschwindigkeit dem Gasstrom entgegenbewegt wird, die zwischen den Wanderungsgeschwindigkeiten der zu trennenden Gaskomponenten liegt.1. Process for the continuous separation of gas mixtures containing a carrier gas according to the principle of gas elution chromatography, characterized in that Column material is moved against the gas flow at a speed between the Migration speeds of the gas components to be separated lies. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Geschwindigkeit des Säulenmaterials gleich dem Mittelwert der Wanderungsgeschwindigkeiten zweier voneinander zu trennender Gaskomponenten . eines Gasgemisches ist.2. The method according to claim 1, characterized in that the speed of the column material equal to the mean value of the migration speeds two gas components to be separated from each other. a gas mixture is. In Betracht gezogene Druckschriften:Considered publications: USA.-Patentschrift Nr. 2 635 706;U.S. Patent No. 2,635,706; Uli mann, Enzyklopädie der Techn. Chemie,
Bd. 1, 1951, S. 356 und 357;
Uli mann, Encyclopedia of Techn. Chemistry,
Vol. 1, 1951, pp. 356 and 357;
Zeitschrift »Erdöl u. Kohle«, 9 (1956), S. 593
bis 597;
Journal "Erdöl u. Coal", 9 (1956), p. 593
to 597;
VDI-Zeitschrift, 98, 1956, Nr. 20 (11. Juli),
S. 1056.
VDI-Zeitschrift, 98, 1956, No. 20 (July 11th),
P. 1056.
DEP20395A 1958-03-26 1958-03-26 Process for the continuous separation of gases according to the principle of gas elution chromatography Pending DE1281400B (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (1)

* Cited by examiner, † Cited by third party
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

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