Production of middle distillate in a dual-bed reactor from synthesis gas through wax cracking: Effect of acid property of Pd-loaded solid acid catalysts on the wax conversion and middle distillate selectivity-Reference-Cited by-同舟云学术

Production of middle distillate in a dual-bed reactor from synthesis gas through wax cracking: Effect of acid property of Pd-loaded solid acid catalysts on the wax conversion and middle distillate selectivity

Published:2008-09 Issue:3-4 Volume:83 Page:195-201
ISSN:0926-3373
Container-title:Applied Catalysis B: Environmental
language:en
Short-container-title:Applied Catalysis B: Environmental

Author:

Cho Kyung Min,Park Sunyoung,Seo Jeong Gil,Youn Min Hye,Baeck Sung-Hyeon,Jun Ki-Won,Chung Jin Suk,Song In Kyu

Publisher

Elsevier BV

Subject

Process Chemistry and Technology,General Environmental Science,Catalysis

Reference54 articles.

1. Iso-paraffins synthesis from modified Fischer–Tropsch reaction—Insights into Pd/beta and Pt/beta catalysts

2. Advances in the Development of Novel Cobalt Fischer−Tropsch Catalysts for Synthesis of Long-Chain Hydrocarbons and Clean Fuels

3. Short history and present trends of Fischer–Tropsch synthesis

4. Modern refining concepts—an update on naphtha-isomerization to modern gasoline manufacture

5. Three-component hybrid catalyst for direct synthesis of isoparaffin via modified Fischer–Tropsch synthesis

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