发明名称 |
Systems and methods for producing substitute natural gas |
摘要 |
Systems and methods for processing a hydrocarbon are provided. The method can include gasifying a feedstock within a gasifier to provide a raw syngas. The raw syngas can be processed within a purification system to provide a treated syngas. A first portion of the treated syngas can be converted into a first effluent in a first methanator. The first effluent can be mixed with a second portion of the treated syngas to provide a first mixed effluent. The first mixed effluent can be converted into a second effluent in a second methanator. The second effluent can be mixed with a third portion of the treated syngas to provide a second mixed effluent. The second mixed effluent can be converted into a third effluent in a third methanator. |
申请公布号 |
US9157043(B2) |
申请公布日期 |
2015.10.13 |
申请号 |
US201213663993 |
申请日期 |
2012.10.30 |
申请人 |
KELLOGG BROWN & ROOT LLC |
发明人 |
Ariyapadi Siva;Shires Philip |
分类号 |
C10J3/00;C10J3/54;C10L3/08;C10J3/48;C10J3/56;C10K1/00;C10K1/02;C10K3/04;C10G2/00;C10K3/00 |
主分类号 |
C10J3/00 |
代理机构 |
|
代理人 |
Machetta Gary M. |
主权项 |
1. A method for processing a hydrocarbon, comprising:
gasifying a feedstock within a gasifier to provide a raw syngas; processing the raw syngas within a purification system to provide a treated syngas; converting a first portion of the treated syngas into a first effluent in a first methanator; mixing the first effluent with a second portion of the treated syngas to provide a first mixed effluent; converting the first mixed effluent into a second effluent in a second methanator; mixing the second effluent with a third portion of the treated syngas to provide a second mixed effluent; converting the second mixed effluent into a third effluent in a third methanator; converting at least a portion of the third effluent into a fourth effluent in a fourth methanator; and wherein the first methanator comprises a first catalyst, the second methanator comprises a second catalyst, the third methanator comprises a third catalyst, and the fourth methanator comprises a fourth catalyst, and wherein the fourth catalyst is a different type of catalyst than the first, second, and third catalysts. |
地址 |
Houston TX US |