Method for coprocessing glycerol and heavy oil in hydrothermal mode to simultaneously obtain lactic acid and light oil
A technology of co-processing and glycerin, which is applied in the field of waste recycling technology and energy, can solve the problems of low hydrogen partial pressure, unsatisfactory effect, high production cost, etc., and achieve the effect of reducing the coking rate
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1-4
[0028] In the autoclave reactor, add alkali NaOH, 20wt%, and 70wt% glycerin according to the mass percentage of water, and then mix it with vacuum heavy oil at a volume ratio of 1:1, and put it into the reactor. The reaction temperature is 200°C, and the pressure is 2Mpa. After reacting for different time, take it out and cool it to room temperature with water. The product analysis results are shown in Table 1.
[0029] Table 1
[0030]
Embodiment 5-7
[0032] In the autoclave reactor, add alkali NaOH, 20wt%, and 70wt% glycerin according to the mass percentage of water, and then mix it with vacuum heavy oil at a volume ratio of 1:1, and put it into the reactor. Pressure 2Mpa, reaction time 3h at different temperatures, product analysis results are shown in Table 2.
[0033] Table 2
[0034]
Embodiment 8-10
[0036] In the autoclave reactor, add alkali NaOH, 20wt%, and 70wt% glycerin according to the mass percentage of water, and then mix it with vacuum heavy oil at a volume ratio of 1:10, and put it into the reactor. The reaction temperature was 350°C, the reaction time was 3 hours, and the pressure conditions were changed by different filling ratios. The product analysis results are shown in Table 3.
[0037] table 3
[0038]
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 


