Production of aromatics-rich higher hydrocarbons from solid biomass
A technology of solid biomass and biomass, applied in the field of conversion of biomass to hydrocarbons
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Embodiment 1-3、5-6
[0100] 100% zeolite extrudates were prepared according to the general procedure described in US 5558851, US 6261545 and US 6632415, where the reaction mixture contained only enough water to allow extrusion. Silica ( 233 or ) with sodium aluminate, sodium hydroxide (5N), water and optionally tetrapropylammonium bromide and seed crystals (for example, ZSM-5 Zeolyst CBV 3024E from Zeolyst International, added at 3% w relative to dry ingredients) Combine in a heated double-arm mixer. The molar composition ranges of the mixtures used in these formulations are as follows.
[0101] SiO 2 / Al 2 o 3 =23-38
[0102] TPA+ / SiO2 2 =0–0.02
[0103] OH- / SiO 2 =0.095-0.225
[0104] Na+ / SiO 2 =0.095-0.225
[0105] h 2 O / SiO 2 =4.8-8.2
[0106] Continue heating and mixing until the mixture is dry to extrudable. The LOI (volatiles measured at 550°C) of the mixture before extrusion ranged from 44-60%. The mixture was then extruded through a 1 / 16 inch die using a Bonnot extruder...
Embodiment A-
[0111] Example A- F: condensation
[0112]The model feed was prepared from water, 2-propanol, THF, acetone, acetic acid, 1,3 propanediol in a weight ratio of 70:15:7:4:3:1. The feed was continuously passed through the catalyst bed with the catalysts of Table 2 as described below, with frequent regeneration by coke combustion. All reactions were performed at a temperature of 375°C, a nitrogen pressure of 100 psig, and a flow rate of 1 WHSV based on the total feed to a 1 / 2 inch by 10 inch reactor bed operated downflow. Sampling reaction twice a day, coke burning 1-2 times / week. The reaction is stopped when the catalyst stops producing significant fuel (organic phase of the product leaving the reaction bed) or the fuel quality is low (low aromatics, high olefin content, etc.). The product contains an organic phase and an aqueous phase (total product is a combination of organic and aqueous phases).
[0113] The catalysts of Examples A-F are provided as follows:
[0114] Comp...
Embodiment 1
[0116] Catalyst for Test C - Example 6
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