31results about How to "Lower liquefaction costs" patented technology

The invention discloses a method for direct liquefaction of biomass. The method includes the following steps: (1) mixing the biomass, a hydrogenation catalyst and a hydrogen donor solvent to obtain abiomass slurry; (2) performing first liquefaction reaction on the biomass slurry and hydrogen to collect a first reaction product; (3) performing second liquefaction reaction on the first reaction product and hydrogen to collect a second reaction product; (4) performing first gas-liquid separation on the second reaction product at 290 to 460DEG C to collect a first liquid phase and a first gas phase; (5) performing second gas-liquid separation on the first gas phase at 30DEG C to 60DEG C to collect a second liquid phase, and mixing the first liquid phase and the second liquid phase to obtain aliquid phase; (6) performing first distillation on the liquid phase to collect a light fraction and a heavy fraction; and (7) performing second distillation on the heavy fraction to separate distillate oil and residue, wherein the light fraction and the distillate oil are liquefied liquids. The liquid yield obtained by the method is high, and the residual solid content in the liquids is low.

The invention discloses a method for direct liquefaction of biomass. The method comprises the following steps: (1) mixing biomass, a hydrogenation catalyst and a hydrogen-donating solvent to prepare a biomass slurry; (2) performing a first liquefaction reaction on the biomass slurry and hydrogen, and collecting the first reaction product; (3) carry out the second liquefaction reaction of the first reaction product and hydrogen, and collect the second reaction product; (4) carry out the first gas-liquid separation on the second reaction product at 290-460 ° C, and collect the first liquid phase and the second reaction product A gas phase; (5) performing a second gas-liquid separation on the first gas phase at 30-60°C, collecting the second liquid phase, mixing the first liquid phase and the second liquid phase to obtain a liquid phase; (6) performing a liquid phase on the liquid phase The first distillation collects the light distillate and the heavy distillate; (7) performs the second distillation on the heavy distillate to separate the distillate oil and residue, and the light distillate and distillate oil are liquids obtained from liquefaction. The yield of the liquid obtained by the above method is high, and the residue solid content in the liquid is low.

The invention relates to the technical field of clean energy, in particular to a process for smelting coal and biomass. The coal and biomass materials are subjected to 'crushing, compression and crushing again' treatment, and biomass coal oil slurry with high solid content and capable of being conveying stably by a pump is successfully obtained. The biomass coal oil slurry is subjected to first liquefaction reaction and second liquefaction reaction sequentially, so that the fact that the biomass is completely liquefied into liquid phase and the yield of the liquid is increased; through twice gas and liquid separation, oil products are enriched and the residues in the oil products are enriched and caked; and through first distillation and second distillation, the yield of the liquid oil isfurther increased, the residues in the liquid oil is further enriched and caked and is discharged to the outside through the bottom of a distillation device, the residues are prevented from entering the subsequent process and the residue solid content of the liquid oil is reduced; and through test, the yield of the liquid oil is above 98 percent by weight and the residue solid content of the liquid oil is less than 0.5 percent by weight.

The invention relates to a method and system for stably supplying air with low energy consumption. According to the method, at least part of each of first heat exchange airflow, second heat exchange airflow and third heat exchange airflow is treated to obtain first airflow to be supplied and second airflow to be supplied. The system comprises a piston air booster, an efficient postcooler, a booster expansion turbine, a main heat exchanger with five separated fluid loops, an upper rectifying tower body, a lower rectifying tower body, a subcooler with four separated fluid pipes, a low-temperature liquid nitrogen and a low-temperature liquid nitrogen. Originally-wasted nitrogen generated by air separation is liquefied, the liquefaction cost of nitrogen is reduced as the cooling capacity of liquid nitrogen is fully utilized, benefits generated by the liquid nitrogen basically offset the cost increased by use of the liquid nitrogen, and the overall energy consumption is reduced on the whole.

The invention relates to a novel method for liquefying a plant biomass and waste polyester mixed supercritical fluid, which comprises the following steps of placing plant biomass, polyester, a catalyst and a liquefying agent into a reaction kettle with a stirrer, raising the temperature of the reaction kettle to 230-280 DEG C, pressurizing to 5-8MPa, preserving the temperature under the state for5-40min, introducing cooling water when being naturally cooled to 100 DEG C after the liquefying is finished to cool the reaction kettle to room temperature; filtering reactant mixture in the reaction kettle by using a Buchner funnel; extracting obtained filtrate and residue by using an organic solvent; and distilling obtained extract liquor and extract by using a rotary evaporator, wherein the product remained in a distillation flask after the distillation is the biomass liquefied oil. The invention develops a new way of utilizing the plant biomass and the waste polyester, realizes the moderation of the liquefying condition of the plant biomass, improves the quality of the biological oil because of the molecular weight of the biological oil is lower, and improves the utilization efficiency of the plant biomass and the waste polyester.