Zobrazeno 1 - 10
of 24
pro vyhledávání: '"Xiaosu Lang"'
Publikováno v:
Industrial & Engineering Chemistry Research. 44:6038-6044
Fischer-Tropsch synthesis (FTS) was studied on a precipitated iron catalyst in a fixed-bed reactor under both supercritical (propane or n-hexane as supercritical fluids; P = 4.1-7.0 MPa) and conventional operating conditions (P = 1.48 MPa), as well a
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d5cc05cf39546d09274172da347a7706
https://doi.org/10.1021/ie0492146
https://doi.org/10.1021/ie0492146
Publikováno v:
Energy Sources. 23:417-425
A 5 L membrane bioreactor system has been designed and operated at low temperature to hydrolyze starch granules directly to sugars using barley α-amylase. The system includes a temperature and pH controlled, well-mixed bioreactor; microfilters to se
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2fb2136155da80c7398bd7bf5f7de29f
https://doi.org/10.1080/009083101300058408
https://doi.org/10.1080/009083101300058408
Publikováno v:
Applied Catalysis A: General. 186:255-275
Effects of pretreatment procedures, using H2, CO, and syngas (H2/CO = 2/3) as reductants, on the performance (activity, selectivity and stability with time) of a precipitated iron catalyst (100 Fe/3 Cu/4 K/16 SiO2 on a mass basis) during Fischer–Tr
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::0ec4e5d34e17775d1dd8abf8455237ff
https://doi.org/10.1016/s0926-860x(99)00148-9
https://doi.org/10.1016/s0926-860x(99)00148-9
Autor:
Xiaosu Lang, Dragomir B. Bukur
Publikováno v:
Industrial & Engineering Chemistry Research. 38:3270-3275
A precipitated iron Fischer−Tropsch (F−T) catalyst (100 Fe/3 Cu/4 K/16 SiO2 on mass basis) was tested in a stirred tank slurry reactor under reaction conditions representative of industrial practice using CO-rich synthesis gas (260 °C, 1.5−2.2
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::cbd4b37a521927bcadd8c5c1025ef92b
https://doi.org/10.1021/ie990028n
https://doi.org/10.1021/ie990028n
Publikováno v:
Industrial & Engineering Chemistry Research. 36:2580-2587
A precipitated iron catalyst (100 Fe/5 Cu/4.2 K/25 SiO2 on mass basis) was tested in a fixed-bed reactor under a variety of process conditions during conventional Fischer−Tropsch synthesis (FTS) and supercritical Fischer−Tropsch synthesis (SFTS).
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::ab173f2f37948bb3ac58ce7bba934a81
https://doi.org/10.1021/ie960507b
https://doi.org/10.1021/ie960507b
Publikováno v:
Journal of Catalysis. 155:366-375
Effects of pretreatment conditions on catalyst performance (activity, selectivity, and stability with time) during Fischer-Tropsch (FT) synthesis were studied in a fixed-bed reactor using a commercial precipitated iron catalyst (100 Fe/5 Cu/4.2 K/25
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d8de37a3fb68b232c5dac4617fb6bcd6
https://doi.org/10.1006/jcat.1995.1218
https://doi.org/10.1006/jcat.1995.1218
Publikováno v:
Energy & Fuels. 9:620-629
Effects of pretreatment procedures, using H 2 , CO, and syngas (H2/CO = 0.7) as reductants, on the performance (activity, selectivity, and stability with time) of a precipitated iron catalyst (100 Fe/5 Cu/4.2 K/16 SiO 2 on a mass basis) during Fische
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::796079a01e01cb641d034d40741236d1
https://doi.org/10.1021/ef00052a008
https://doi.org/10.1021/ef00052a008
Publikováno v:
Catalysis Today. 24:111-119
A precipitated iron catalyst (100 Fe/0.3 Cu/0.8 K) was tested in a fixed-bed reactor and a stirred tank slurry reactor at 250–260°C, 1.48 MPa, 2 Nl g-cat−1 h−1, and H2:CO = 2:3. Two different pretreatment procedures were employed (hydrogen red
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d93740ae401253431e7c6b87c633a834
https://doi.org/10.1016/0920-5861(95)00010-d
https://doi.org/10.1016/0920-5861(95)00010-d
Publikováno v:
Applied Catalysis A: General. 126:85-113
A doubly promoted precipitated iron catalyst (100 Fe/0.3 Cu/0.8 K by mass) was characterized after different pretreatment conditions and after Fischer-Tropsch (FT) synthesis in a fixed bed reactor. The BET surface area of the catalyst decreased marke
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::db5e76f5a179c830305a63ed592bdf86
https://doi.org/10.1016/0926-860x(95)00020-8
https://doi.org/10.1016/0926-860x(95)00020-8
Publikováno v:
Industrial & Engineering Chemistry Research. 34:72-77
Fischer-Tropsch synthesis (FTS) on a precipitated iron catalyst was conducted in a fixed bed reactor at baseline conditions of 1.48 MPa, 250 C, 2 L(NTP)/(h [times] g of cat), H[sub 2]/CO = 0.67, and in supercritical propane (total pressure of 7 MPa)
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::cf7458cef161e6e2945d7e9f161ff4e1
https://doi.org/10.1021/ie00040a004
https://doi.org/10.1021/ie00040a004