发明名称 |
DIRECT COAL LIQUEFACTION PROCESS |
摘要 |
A direct coal liquefaction method and apparatus in which the feed coal is mixed with a recycled 600° F.+ non-donor stream in which the ratio of coal to said stream is at least 1.5:1 on a moisture free basis to form an input slurry to a DCL reactor. Hydrogen containing treat gas is supplied to the reactor. 1000° F.− bottoms from the reactor are recycled as part of the 600° F.+ non-donor stream. 1000° F.+ bottoms from the reactor are gasified in a PDX unit to provide hydrogen for the DCL reaction. The ratio of recycled bottoms to feed coal is between 1:0.5 and 1:1.5. |
申请公布号 |
US2015191657(A1) |
申请公布日期 |
2015.07.09 |
申请号 |
US201414147542 |
申请日期 |
2014.01.05 |
申请人 |
ACCELERGY CORPORATION |
发明人 |
Bauman Richard F.;Maa Peter S. |
分类号 |
C10G1/06 |
主分类号 |
C10G1/06 |
代理机构 |
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代理人 |
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主权项 |
1) A method for producing liquids from feed coal, comprising the steps of:
a) mixing a feed coal having an greater than 12% inertinite content with a non-donor stream that includes a recycled 600° F.+ fraction of the product from a direct coal liquefaction (DCL) slurry reactor to form a feed coal slurry, the ratio of non-donor stream to feed coal being greater than 1.6:1 on a moisture free basis; b) supplying said feed coal slurry to said DCL slurry reactor; c) adding a molybdenum or iron containing microcatalyst to the input of the DCL reactor; and d) supplying H2 containing treat gas to the DCL reactor. |
地址 |
Houston TX US |