Carbon dioxide capture for the oxidative coupling of methane process - A case study in mini-plant scale

Chemical Engineering Research and Design

Volumn 89, Issue 8, 2011, Pages 1261-1270

  Stunkel S ^a   Drescher, A ^a   Wind, J ^b   Brinkmann, T ^b   Repke, J U ^a   Wozny, G ^a  

^a Institute of Propulsion Technology   (Germany)

^b INSTITUTE OF MATERIALS RESEARCH   (Germany)

Author keywords

Absorption; Carbon dioxide capture; Hybrid process; Membrane; Oxidative coupling of methane

Indexed keywords

ABSORPTION PROCESS; ASPEN PLUS; CARBON DIOXIDE CAPTURE; CHEMICAL ABSORPTION; CHEMICAL EQUILIBRIUMS; CONCENTRATION POLARIZATION; DENSE MEMBRANE; DESIGN TASKS; ELECTROLYTE-NRTL; ENERGETIC PROCESS; ENERGY EFFICIENT; EXPERIMENTAL STUDIES; GAS PERMEATION; GAS STREAMS; HYBRID PROCESS; HYBRID SEPARATION PROCESS; JOULE-THOMSON EFFECT; KINETIC REACTIONS; MEMBRANE MODULE; MONOETHANOLAMINE; OIL BASED; OPERATION PRESSURE; OXIDATIVE COUPLING OF METHANE; PRODUCT GAS; PRODUCT STREAMS; RATE BASED MODEL; SOLUTION-DIFFUSION MODEL; STAND -ALONE; STATE OF THE ART;

ABSORPTION; CARBON DIOXIDE; ETHYLENE; METHANE; PERMEATION; PETROLEUM REFINING; PURIFICATION; REFINING; THERMOELECTRICITY;

GAS PERMEABLE MEMBRANES;

EID: 79958732903     PISSN: 02638762     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.cherd.2011.02.024     Document Type: Article

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