Catalyst for selective hydrogenation olefin removal of reformed oil
A catalyst and oil-generating technology, applied in the field of oil hydrogenation, can solve the problems of poor catalyst stability, short operation period, low processing capacity, etc., and achieve the effects of high reduction degree, reduced residence time, and low reaction temperature
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0050] (1) Add 1L of deionized water into the reaction tank as the bottom liquid, put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively, and control the temperature of the reaction tank at 60°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 10 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 8.0, and the neutralization was completed after 120 min. In the reaction tank at a constant temperature of 85°C and a constant pH value of 8.5, aging treatment for 5 hours, and then washing with deionized water for 3 times, after filtration, the filter cake was mixed with deionized water and stirred evenly to obtain pseudo-boehmite sol, wherein The solid content is 0.5 g / mL as alumina. Add Y-type molecular sieves to the pseudo-boehmite sol, then add the above mixture into the autoclave, conduct hydrotherm...
Embodiment 2
[0056] (1) Add 1L of deionized water into the reaction tank as the bottom liquid, put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively, and control the temperature of the reaction tank at 70°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 10 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 7.5, and the neutralization was completed after 120 min. In the reaction tank at a constant temperature of 80°C and a constant pH value of 8.5, aging treatment for 5 hours, and then washing with deionized water for 3 times, after filtration, the filter cake was mixed with deionized water and stirred evenly to obtain pseudo-boehmite sol, wherein The solid content is 0.6g / mL in terms of alumina. Add Y-type molecular sieves to the pseudo-boehmite sol, then add the above mixture into a high-pressure reactor, ...
Embodiment 3
[0062] (1) Add 1L of deionized water into the reaction tank as the bottom liquid, put 1L of aluminum sulfate solution and 1L of sodium hydroxide solution into the raw material tank respectively, and control the temperature of the reaction tank at 80°C. The aluminum sulfate solution was injected into the reaction tank at a rate of 10 mL / min, while the sodium hydroxide solution was injected and the rate was adjusted to keep the pH value of the reaction tank solution constant at 7.5, and the neutralization was completed after 120 min. In the reaction tank at a constant 90°C and a constant pH value of 8.0, aging treatment for 5 hours, and then washing with deionized water for 3 times, after filtration, the filter cake was mixed with deionized water and stirred evenly to obtain pseudo-boehmite sol, wherein The solid content is 0.5 g / mL as alumina. Add Y-type molecular sieves to the pseudo-boehmite sol, then add the above mixture into a high-pressure reactor, conduct hydrothermal tr...
PUM
| Property | Measurement | Unit |
|---|---|---|
| dispersity | aaaaa | aaaaa |
| dispersity | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More