Method for upgrading the quality of high olefin catalytic cracking gasoline
A technology for catalytic cracking of gasoline and high olefins, applied in the treatment of hydrocarbon oil, hydrocarbon oil treatment products, petroleum industry, etc., can solve the problems of high octane number loss, insignificant and small effect, and most of them still need hydrotreating.
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0072] 1. Preparation of aromatization catalyst
[0073] 1) Preparation of catalyst precursor
[0074] At room temperature, the nanoscale HZSM-5 molecular sieve with a silicon-aluminum ratio of 25 and pseudo-boehmite were physically mixed in a ratio of 4:1 to obtain a catalyst precursor.
[0075] 2) Ion exchange modification
[0076] The catalyst precursor was ion-exchanged by the constant temperature water bath method, specifically, sodium hydroxide was dissolved in deionized water, mixed with the catalyst precursor and placed in a water bath at 90°C for 2 hours, so that the loading capacity of sodium was about 0.2 % by weight, followed by drying at about 120°C for about 8 hours and firing at about 540°C for about 4 hours.
[0077] 3) The first modification treatment
[0078] Using the equal-volume impregnation method, the first modification treatment is carried out on the catalyst precursor treated by ion exchange, specifically, dissolving ammonium dihydrogen phosphate in d...
Embodiment 2
[0095] 1. Preparation of aromatization catalyst
[0096] 1) Preparation of catalyst precursor
[0097] At room temperature, the nanoscale HZSM-5 molecular sieve with a silicon-to-aluminum ratio of 25 and pseudo-boehmite were physically mixed at a ratio of 9:1 to obtain a catalyst precursor.
[0098] 2) Ion exchange modification
[0099] The catalyst precursor was ion-exchanged by using a constant temperature water bath method, specifically dissolving sodium hydroxide in deionized water, mixing it with the catalyst precursor, and stirring it in a water bath at 90°C for 2 hours, so that the loading capacity of sodium was about 0.5 % by weight, followed by drying at about 120°C for about 8 hours and firing at about 540°C for about 4 hours.
[0100] 3) The first modification treatment
[0101] Using an equal-volume impregnation method, carry out the first modification treatment on the ion-exchange-treated catalyst precursor, specifically dissolving lanthanum nitrate in deionize...
Embodiment 3
[0118] like figure 1 As shown, the method for upgrading the quality of high olefin catalytic cracking gasoline in this embodiment includes the following steps:
[0119] 1. Prehydrogenation
[0120] The composition of the high olefin catalytic cracking gasoline feedstock in this example is shown in Table 5.
[0121] Table 5 Composition of High Olefin Catalytic Cracking Gasoline Feedstock
[0122]
[0123] In the presence of a pre-hydrogenation catalyst, pre-hydrogenate the above-mentioned high-olefin catalytic cracking gasoline to obtain pre-hydrogenation catalytic cracking gasoline; wherein the pre-hydrogenation catalyst is Ni-Mo / Al 2 o 3 , which consists of (mass content%): Al 2 o 3 90.5%, Ni6%, Mo 3.5%; pre-hydrogenation process conditions: hydrogen partial pressure 2.2MPa, volume space velocity 3.0h -1 , the volume ratio of hydrogen to oil is 10:1, and the reaction temperature is 110°C.
[0124] After the above-mentioned prehydrogenation, the light sulfur compoun...
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