A method for comprehensive utilization of lignocellulosic biomass to prepare energy chemicals
A lignocellulose and biomass technology, applied in biochemical equipment and methods, lignin derivatives, microbial-based methods, etc., can solve problems such as waste of resources, achieve cost savings, improve economy, and improve stability Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0034] Biomass multi-component separation:
[0035] Take 10kg of corn cob powder (less than 20 mesh), add dilute sulfuric acid aqueous solution (concentration: 0.1 mol / liter) and treat at 80°C for 12 hours according to the material / solution ratio of 1:6 (dry weight), filter, and add sodium hydroxide to the filtrate , adjust the pH value to 6.5 to obtain xylose hydrolyzate (pentose sugar content 5%);
[0036] Add NaOH solution (concentration 0.5 mol / liter) to the solid material obtained by filtration, and treat it at 50°C for 6 hours according to the material / solution ratio of 1:10 (dry weight) to dissolve and separate lignin. Then filter and wash the solid material to a pH value of 8, resulting in 5 kg of cellulose material (dry basis weight);
[0037]Hydrochloric acid was added to the NaOH filtrate containing lignin to adjust the pH value to 6.5, and the precipitate was filtered to obtain 1.5 kg (dry weight) of a solid lignin product.
[0038] Biological fermentation proces...
Embodiment 2
[0048] The conditions for the catalytic conversion of cellulose were the same as in Example 1, except that the hydrogenation catalyst 0.5%Ru-10%Ni / AC was replaced by 0.2%Ru-Raney Ni, and the dosage was reduced to 0.15kg. After the reaction, the yield of ethylene glycol was 48%, and the yield of propylene glycol was 8%. It is shown that the two hydrogenation catalysts have similar catalytic performance.
Embodiment 3
[0053] Catalyst stability test: The conditions for cellulose catalytic conversion are the same as in Example 2, except that the hydrogenation catalyst is replaced by a fresh 0.2% Ru-Raney Ni catalyst with the recovered catalyst 0.2% Ru-Raney used once in Example 2 Ni. After the reaction, the yield of ethylene glycol was 47%, and the yield of propylene glycol was 8%.
[0054] It can be seen that the activity of the 0.2% Ru-Raney Ni catalyst has no obvious attenuation during repeated use and has good stability.
PUM
| Property | Measurement | Unit |
|---|---|---|
| diameter | aaaaa | aaaaa |
| length | aaaaa | aaaaa |
Abstract
Description
Claims
Application Information
Login to View More