公开(公告)号：US10507462B2

公开(公告)日：2019-12-17

申请号：US15798333

申请日：2017-10-30

Applicant: UOP LLC

Inventor： Pelin Cox ,  William D. Schlueter ,  William Yanez ,  Jeffrey Grott

IPC: B01J38/04 ,  B01J8/12 ,  B01J38/02 ,  B01J38/10 ,  B01J29/90

Abstract: A process is disclosed for an improved catalyst stripping process. The stripping vessel is divided into two zones. The first zone is a stripping zone where a substantial portion of the volatile hydrocarbons is removed at higher severity conditions. After the catalyst is stripped, the stripped catalyst moves to the lower cooling zone to be cooled at lower severity conditions. The flow rates, temperatures, pressures and the stripping and cooling zones are designed to ensure there is minimal volatile hydrocarbons on the catalyst by the time it leaves the stripping vessel. This design enables efficient stripping of volatile hydrocarbons at high severity conditions and eliminates these components from being stripped off elsewhere in the unit causing process and equipment issues.

公开(公告)号：US20180050334A1

公开(公告)日：2018-02-22

申请号：US15798333

申请日：2017-10-30

Applicant: UOP LLC

Inventor： Pelin Cox ,  William D. Schlueter ,  William Yanez ,  Jeffrey Grott

IPC: B01J38/04 ,  B01J38/02 ,  B01J8/12

CPC classification number: B01J38/04 ,  B01J8/125 ,  B01J29/90 ,  B01J38/02 ,  B01J38/10 ,  C10G2300/4093

Abstract: A process is disclosed for an improved catalyst stripping process. The stripping vessel is divided into two zones. The first zone is a stripping zone where a substantial portion of the volatile hydrocarbons is removed at higher severity conditions. After the catalyst is stripped, the stripped catalyst moves to the lower cooling zone to be cooled at lower severity conditions. The flow rates, temperatures, pressures and the stripping and cooling zones are designed to ensure there is minimal volatile hydrocarbons on the catalyst by the time it leaves the stripping vessel. This design enables efficient stripping of volatile hydrocarbons at high severity conditions and eliminates these components from being stripped off elsewhere in the unit causing process and equipment issues.

公开(公告)号：US20160289140A1

公开(公告)日：2016-10-06

申请号：US14674832

申请日：2015-03-31

Applicant: UOP LLC

Inventor： Robert J. Schmidt ,  Deng-Yang Jan ,  Pelin Cox

IPC: C07C2/66 ,  C07C7/148

CPC classification number: C07C2/66 ,  B01J29/08 ,  B01J29/70 ,  B01J29/7007 ,  B01J29/7038 ,  B01J29/80 ,  B01J2229/42 ,  C01B39/48 ,  C07C7/148 ,  C07C2529/70 ,  C07C2529/80 ,  Y02P20/52 ,  C07C15/085 ,  C07C15/073

Abstract: A method for alkylation of a feedstock is described. The method includes contacting the feedstock comprising at least one alkylatable aromatic compound and an alkylating agent with a first alkylating catalyst composition under alkylating conditions, the first alkylating catalyst composition comprising UZM-8 zeolite and a binder, the first alkylating catalyst composition having 2-20 wt % UZM-8 zeolite and the catalyst having a nitrogen to zeolite aluminum molar ratio of between about 0.01 to about 0.040; wherein a total alkylated selectivity at a temperature and a molar ratio of alkylatable aromatic compound to alkylating agent is greater than 99.0%.

Abstract translation: 描述了原料烷基化的方法。 该方法包括在烷基化条件下将包含至少一种可烷基化芳族化合物和烷基化剂的原料与第一烷基化催化剂组合物接触，所述第一烷基化催化剂组合物包含UZM-8沸石和粘合剂，第一烷基化催化剂组合物具有2-20 重量％的UZM-8沸石和具有约0.01至约0.040的氮与沸石铝摩尔比的催化剂; 其中烷基化芳族化合物与烷基化剂的温度和摩尔比的总烷基化选择性大于99.0％。

公开(公告)号：US20160176778A1

公开(公告)日：2016-06-23

申请号：US14574293

申请日：2014-12-17

Applicant: UOP LLC

Inventor： Deng-Yang Jan ,  Pelin Cox

IPC: C07C2/76

CPC classification number: C07C2/76 ,  C07C2/66 ,  C07C2523/08 ,  C07C2529/06 ,  C07C2529/068 ,  C07C2529/076 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08

Abstract: A process is disclosed for the aromatization of light aliphatic hydrocarbons, such as propane, into aromatic hydrocarbons. The process provides increased aromatics production, decreasing methane and ethane production, coke fouling and decreasing heavy aromatics. This improvement for the aromatization of light aliphatic hydrocarbons is achieved by introducing heavier of the light alphatic hydrocarbons in the feed to the lag reactors.

Abstract translation: 公开了一种将轻质脂族烃如丙烷芳构化成芳族烃的方法。 该方法提高了芳烃生产，减少了甲烷和乙烷生产，焦炭结垢和减少了重质芳烃。 对轻质脂肪族烃的芳构化的这种改进是通过将较重的轻质碳氢化合物引入滞后反应器的进料来实现的。