PROCESS FOR OBTAINING CARBON DIOXIDE FROM GASEOUS MIXTURES

A method of purifying gas mixtures containing 85% minium CO2, also water and the more volatile H2, N2, methane, and other less volatile hydrocarbons and H2S consists of: (a) distilling the water at 45-60 atm. and 10 degrees C minimum, (b) separating the less volatile constituents with the water usin...

Ausführliche Beschreibung

Gespeichert in:

Bibliographische Detailangaben
Hauptverfasser:	HATOS PAL, SIMEK REZSOE, BERES FERENC, KRIZA KALMAN GDJA
Format:	Patent
Sprache:	eng
Schlagworte:	BLASTING CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSEGASES [GHG] CHEMISTRY CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS COMBINED HEATING AND REFRIGERATION SYSTEMS COMPOUNDS THEREOF GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS HEAT PUMP SYSTEMS HEATING INORGANIC CHEMISTRY LIGHTING LIQUEFACTION SOLIDIFICATION OF GASES LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS MANUFACTURE OR STORAGE OF ICE MECHANICAL ENGINEERING METALLURGY MIXTURES BY PRESSURE AND COLD TREATMENT NON-METALLIC ELEMENTS REFRIGERATION OR COOLING TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE WEAPONS
Online-Zugang:	Volltext bestellen
Tags:	Tag hinzufügen Keine Tags, Fügen Sie den ersten Tag hinzu!

Beschreibung
Zusammenfassung:	A method of purifying gas mixtures containing 85% minium CO2, also water and the more volatile H2, N2, methane, and other less volatile hydrocarbons and H2S consists of: (a) distilling the water at 45-60 atm. and 10 degrees C minimum, (b) separating the less volatile constituents with the water using a reflux ratio above 0.2, (c) distilling the more volatile constituents using the feed to the column as the downward trickling liquid for rectification; this feed is adjusted to the boiling temp. of CO2 associated with the distillation pressure and to a pressure above distillation pressure. No adsorption dyring of CO2; clogging due to formation of ice and hydrates is eliminated; very exact separation; low plant cost. After distilling the water, the other impurities are separated in two columns, one for the more volatile constituents at 10-35 atm., the other for the less volatile at least 1 atm. higher, but not above 60 atm.