公开(公告)号：US08373013B2

公开(公告)日：2013-02-12

申请号：US12373586

申请日：2007-07-12

申请人： Wenhua Xie ,  Genquan Zhu ,  Qiang Fu ,  Zhiguo Wu ,  Shaobing Yu ,  Yihua Yang ,  Qiang Liu ,  Zhiqiang Qiao ,  Xuhong Mu ,  Chaogang Xie ,  Yibin Luo ,  Jiushun Zhang ,  Xingtian Shu

发明人： Wenhua Xie ,  Genquan Zhu ,  Qiang Fu ,  Zhiguo Wu ,  Shaobing Yu ,  Yihua Yang ,  Qiang Liu ,  Zhiqiang Qiao ,  Xuhong Mu ,  Chaogang Xie ,  Yibin Luo ,  Jiushun Zhang ,  Xingtian Shu

IPC分类号： C01C1/20

CPC分类号： C10G11/05 ,  B01J29/084 ,  B01J29/46 ,  B01J29/80 ,  B01J29/90 ,  B01J35/0006 ,  C07C1/20 ,  C07C2521/16 ,  C07C2529/08 ,  C07C2529/70 ,  C07C2529/85 ,  C10G3/49 ,  C10G3/55 ,  C10G3/57 ,  C10G3/62 ,  C10G57/00 ,  C10G2300/1033 ,  C10G2300/1037 ,  C10G2300/104 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/4018 ,  C10G2300/701 ,  C10G2300/708 ,  Y02P20/584 ,  C07C11/02

摘要： A process for combining the catalytic conversion of organic oxygenates and the catalytic conversion of hydrocarbons: an organic oxygenate feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, and a coked catalyst and a product stream are obtained after separating the reaction stream; a hydrocarbon feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, a spent catalyst and a reaction oil vapor are obtained after separating the reaction stream, and the reaction oil vapor is further separated to give the products such as gas, gasoline and the like; a part or all of the coked catalyst and a part or all of the spent catalyst enter the regenerator for the coke-burning regeneration, and the regenerated catalyst is divided into two portions, wherein one portion returns to be contacted with the hydrocarbon feedstock, and the other portion, after cooling, returns to be contacted with the organic oxygenate feedstock. This process not only reasonably utilizes the excessive thermal energy of the hydrocarbon conversion, but also solves the problem of heat supply for the conversion of the organic oxygenate, thus ensuring the continuous catalytic conversion of the organic oxygenate.

摘要翻译： 将有机含氧化合物的催化转化和烃的催化转化与有机含氧化合物原料结合的方法与含Y-沸石的催化剂接触以产生反应流，分离反应后得到结焦催化剂和产物流 流; 将烃原料与含Y-沸石的催化剂接触以产生反应物流，分离反应物流后得到废催化剂和反应油蒸气，反应油蒸气进一步分离，得到产物如气体， 汽油等; 一部分或全部的焦化催化剂和一部分或全部废废催化剂进入再生器进行焦炭燃烧再生，再生催化剂分成两部分，其中一部分返回以与烃原料接触，和 冷却后的另一部分返回以与有机含氧化合物原料接触。 该方法不仅合理地利用烃转化的过量热能，还解决了有机含氧化合物转化的供热问题，从而确保有机含氧化合物的连续催化转化。

公开(公告)号：US20090318742A1

公开(公告)日：2009-12-24

申请号：US12373586

申请日：2007-07-12

申请人： Wenhua Xie ,  Genquan Zhu ,  Qiang Fu ,  Zhiguo Wu ,  Shaobing Yu ,  Yihua Yang ,  Qiang Liu ,  Zhiqiang Qiao ,  Xuhong Mu ,  Chaogang Xie ,  Yibin Luo ,  Jiushun Zhang ,  Xingtian Shu

发明人： Wenhua Xie ,  Genquan Zhu ,  Qiang Fu ,  Zhiguo Wu ,  Shaobing Yu ,  Yihua Yang ,  Qiang Liu ,  Zhiqiang Qiao ,  Xuhong Mu ,  Chaogang Xie ,  Yibin Luo ,  Jiushun Zhang ,  Xingtian Shu

IPC分类号： C07C11/00

CPC分类号： C10G11/05 ,  B01J29/084 ,  B01J29/46 ,  B01J29/80 ,  B01J29/90 ,  B01J35/0006 ,  C07C1/20 ,  C07C2521/16 ,  C07C2529/08 ,  C07C2529/70 ,  C07C2529/85 ,  C10G3/49 ,  C10G3/55 ,  C10G3/57 ,  C10G3/62 ,  C10G57/00 ,  C10G2300/1033 ,  C10G2300/1037 ,  C10G2300/104 ,  C10G2300/1055 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/4018 ,  C10G2300/701 ,  C10G2300/708 ,  Y02P20/584 ,  C07C11/02

摘要： A process for combining the catalytic conversion of organic oxygenates and the catalytic conversion of hydrocarbons: an organic oxygenate feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, and a coked catalyst and a product stream are obtained after separating the reaction stream; a hydrocarbon feedstock is contacted with a Y-zeolite containing catalyst to produce a reaction stream, a spent catalyst and a reaction oil vapor are obtained after separating the reaction stream, and the reaction oil vapor is further separated to give the products such as gas, gasoline and the like; a part or all of the coked catalyst and a part or all of the spent catalyst enter the regenerator for the coke-burning regeneration, and the regenerated catalyst is divided into two portions, wherein one portion returns to be contacted with the hydrocarbon feedstock, and the other portion, after cooling, returns to be contacted with the organic oxygenate feedstock. This process not only reasonably utilizes the excessive thermal energy of the hydrocarbon conversion, but also solves the problem of heat supply for the conversion of the organic oxygenate, thus ensuring the continuous catalytic conversion of the organic oxygenate.

摘要翻译： 将有机含氧化合物的催化转化和烃的催化转化与有机含氧化合物原料结合的方法与含Y-沸石的催化剂接触以产生反应流，分离反应后得到结焦催化剂和产物流 流; 将烃原料与含Y-沸石的催化剂接触以产生反应物流，分离反应物流后得到废催化剂和反应油蒸气，反应油蒸气进一步分离，得到产物如气体， 汽油等; 一部分或全部的焦化催化剂和一部分或全部废废催化剂进入再生器进行焦炭燃烧再生，再生催化剂分成两部分，其中一部分返回以与烃原料接触，和 冷却后的另一部分返回以与有机含氧化合物原料接触。 该方法不仅合理地利用烃转化的过量热能，还解决了有机含氧化合物转化的供热问题，从而确保有机含氧化合物的连续催化转化。