Efficient capture of CO2 from simulated flue gas by formation of TBAB or TBAF semiclathrate hydrates (Record no. 171105)

MARC details
000 -LEADER
fixed length control field 02236nab a2200205 4500
008 - CÓDIGOS DE INFORMACIÓN DE LONGITUD FIJA - INFORMACIÓN GENERAL
Campo de control de longitud fija 260224s2009 xxu
245 00 - TITULO
Título Efficient capture of CO2 from simulated flue gas by formation of TBAB or TBAF semiclathrate hydrates
260 ## - PUBLICACION, DISTRIBUCION, ETC
Lugar de publicación, distribución, etc.
Nombre de publicador, distribuidor, etc.
Fecha de publicación, distribución, etc. jul./ago. 2009
270 ## - FECHA DE CARGA
Fecha de carga 16/06/2010 ; 16/06/2010
300 ## - DESCRIPCION FISICA
Otra extensión 7 p. ; 4202-4208
520 ## - RESUMEN, ETC
Resumen Transcripción del resumen del autor. Capturing CO2 by forming hydrate is an attractive technology for reducing the greenhouse effect. The most primary challenges are high energy consumption, low hydrate formation rate, and separation efficiency. This work presents efficient capture of CO2 from simulated flue gas (CO2 (16.60 mol %)/N2 binary mixtures) by formation of semiclathrate hydrates at 4.5 and 7.1 °C and feed pressures ranging from 2.19 to 7.31 MPa. The effect of 0.293 mol % tetra-n-butyl ammonium bromide (TBAB) and tetra-n-butyl ammonium fluoride (TBAF) on the hydrate formation rate, reactor space velocity, and CO2 separation efficiency was studied in a 1 L stirred reactor. The results showed the hydrate formation rate constant increased with increasing feed pressure and reached the maximum at 2.82 × 10-7 mol2/(s·J) with TBAB and 8.26 × 10-7 mol2/(s·J) with TBAF. The space velocity of the hydrate reactor increased with increasing feed pressure and reached a maximum of 13.46 h-1 with TBAB and 25.96 h-1 with TBAF. CO2 recovery was about 50%, and the optimum CO2 separation factor with TBAF was 36.98, which was about 4 times higher than that with TBAB in the range of feed pressure. CO2 could be enriched to 90.40 mol % from simulated flue gas under low feed pressure by two stages of hydrate separation with TBAF. The results demonstrated that TBAB, especially TBAF, could accelerate hydrate formation. The space velocity of the hydrate reactor with TBAB or TBAF was higher than that with THF. CO2 could be easily enriched in the hydrate phase by two stages of hydrate separation under gentle conditions.
581 ## - ESTADO DE COLECCIÓN
Estado de colección 4
773 0# - CORRECCIÓN
Título Energy & fuels
Partes relacionadas 23
942 ## - DESC. DE MATERIAL
Tipo de item KOHA Artículo de Revista
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Fan, Shuanshi
9 (RLIN) 42838
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Li, Shifeng
9 (RLIN) 42839
100 1# - RESPONSABLE PERSONAL
Apellido, Nombre Wang, Jingqu
9 (RLIN) 42840
Holdings
Biblioteca propietaria Biblioteca actual Fecha de adquisición Inventario Total de préstamos Inventario Fecha de carga Tipo de item KOHA
Biblioteca Alejandro Angel Bulgheroni Biblioteca Alejandro Angel Bulgheroni 05/03/2026 200045963   200045963 05/03/2026 Artículo de Revista


Instituto Argentino del Petróleo y del Gas
Maipú 639 (C1006ACG) – Buenos Aires – Argentina
Tel: (54 11) 5277 IAPG (4274)
Lu - Vie 11 a 17 hs
Mail: biblio@iapg.org.ar


Copyright © 2026, Instituto Argentino del Petróleo y del Gas, todos los derechos reservados.

Protección de datos personales