发明名称 |
Process and reactor for dehydration of butanol to butylenes |
摘要 |
A reactor design and configuration and a process for the catalytic dehydration of butanol to butylenes where the reactor train is comprised of a multi-stage single reactor vessel or multiple reactor vessels wherein each stage and/or vessel has different length, internal diameter, and volume than the other stages and/or vessels and in addition the stages and/or reactor vessels are connected in series or in parallel arrangement, preferably used with an improved means of introducing the butanol feedstock and a heat carrying inert gas to the improved reactor train. |
申请公布号 |
US9340470(B2) |
申请公布日期 |
2016.05.17 |
申请号 |
US201213727024 |
申请日期 |
2012.12.26 |
申请人 |
Petron Scientech Inc |
发明人 |
Taheri Hassan;Sarin Yogendra;Ozero Brian |
分类号 |
B01J8/00;B01J8/02;B01J8/04;C07C1/24;C07C1/20 |
主分类号 |
B01J8/00 |
代理机构 |
|
代理人 |
Moseley Richard L.;Johnson Kenneth H. |
主权项 |
1. An adiabatic reactor train configured for application to the catalytic
(a) dehydration of butanol to butylenes process wherein: (b) the train is comprised of several adiabatic gas phase reactor vessels, (c) the reactor vessels are connected in series or parallel configuration, (d) each reactor vessel has a different internal diameter, length and volume than the other vessels, (e) each reactor vessel contains a quantity of fixed bed catalyst whose amount is different than the quantity in the other vessels, and (f) each vessel is substantially circular. |
地址 |
Princeton NJ US |