Method and device for producing gasoline with high aromatic hydrocarbon content by modifying MTP byproduct mixed aromatic hydrocarbon, and gasoline with high aromatic hydrocarbon content and application thereof
A technology of mixed aromatics and high aromatics, applied in the field of aromatics chemical industry, can solve the problems of unable to quickly increase aromatics content, unstable aromatics content, high investment cost of equipment, etc., achieve the effect of reducing aromatics content, increasing olefin content, and reducing production cost of equipment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment approach
[0049] According to a preferred embodiment of the present invention, the device for producing gasoline with high aromatic content by upgrading the MTP by-product mixed aromatics is as figure 1 As shown, the device includes: a rectification tower, a heating furnace, a fixed-bed reactor, a cooling tower and a product tank connected in sequence; the rectification tower is used for rectifying MTP by-product mixed aromatics to obtain heavy components and Mixed light hydrocarbons with a distillation range <165°C; the heating furnace is used to heat the mixed light hydrocarbons to obtain heated mixed light hydrocarbons; the fixed-bed reactor is used to combine the heated mixed light hydrocarbons with The aromatization catalyst is contacted to perform an aromatization reaction to obtain an aromatization product; the cooling tower is used to cool the aromatization product to obtain gas phase components and gasoline with high aromatic content; the product tank is used for The gasoline w...
Embodiment 1
[0056] (1) The MTP by-product mixed aromatics are rectified in a rectification tower to obtain mixed light hydrocarbons and heavy components with a distillation range <165°C, wherein the theoretical plate number of the rectification tower is 15, and the rectification conditions Including: the reflux ratio is 5:1, the extraction rate is 15mL / min, and the heating rate is 0.5°C / min;
[0057] (2) the mixed light hydrocarbon that step (1) obtains is adjusted space velocity to be 1h -1 , and transported to a 350°C heating furnace by a feed pump at a pressure of 1.5MPa for heating, and then entered into a fixed-bed reactor equipped with a ZSM-5 strip catalyst for aromatization reaction to obtain an aromatization product; wherein, The conditions of the aromatization reaction include: the temperature of the catalyst bed is 450°C, and the temperature of the column core is 460°C;
[0058] (3) cooling the aromatized product obtained in step (2) in a cooler to obtain gasoline S1 with high...
Embodiment 2
[0063] (1) Rectify MTP by-product mixed aromatics in a rectification tower to obtain mixed light hydrocarbons and heavy components with a distillation range <165°C, wherein the theoretical plate number of the rectification tower is 30, and the rectification conditions Including: the reflux ratio is 8:1, the extraction rate is 25mL / min, and the heating rate is 0.5°C / min;
[0064] (2) the mixed light hydrocarbon that step (1) obtains is adjusted space velocity to be 1h -1 , and transported to a 300°C heating furnace by a feed pump at a pressure of 1.5 MPa for heating, and then entered into a fixed-bed reactor equipped with a ZSM-5 strip catalyst for aromatization reaction to obtain an aromatization product; wherein, The conditions of the aromatization reaction include: the temperature of the catalyst bed is 350°C, and the temperature of the column core is 360°C;
[0065] (3) cooling the aromatized product obtained in step (2) in a cooler to obtain gasoline S2 with high aromatic...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com