33results about How to "Wide adaptability of raw materials" patented technology

The invention discloses a kind of biomass gasifying method and device. The technology through separating the two courses of solid biomass pyrogenation and decomposition and gasification of the pyrogenation outcome, then transform the biomass into flammable gas of rather low tar content. Firstly send biomass into the pyrogenation reactor, without oxidant in; have pyrogenation reaction at 400 - 650 Deg. C, the pyrogenation outcome including pyrogenation gas and remaining charcoal gets into pyrogenation carburetor, and have incomplete oxidizing combustion reaction with sent oxidant, to form a high temperature of 900 - 1100 Deg. C. At the time, the heavy hydrocarbon substance of tar decomposes into small molecule gas, and the decomposed gas leaves out of the carburetor after having deoxidizing reaction with the nether blazing carbon layer. The high temperature gas is provided for consumers' use after depurated and cooled. The gas produced by the invention has very low tar content, which makes the following depurating equipment simple, won't produce second pollution and makes the raw materials widely used. The produced fuel gas can be used in civil filed and directly used for generating electricity.

The invention discloses a combined process method for treating inferior residual oil. The method comprises the following steps: a residual oil material enters a solvent deasphalting device to obtain DAO and deoil asphalt; the obtained DAO enters a hydrogenation device of a boiling bed and is treated to obtained a lightweight distillation fraction and hydrogenated tail oil; the hydrogenated tail oil enters a catalytic cracking device and is treated to obtain a lightweight distillation fraction and oil slurry; at least partial oil slurry and the deoil asphalt are mixed, enter a hydrogenation device of a suspension bed and are treated to obtain a lightweight distillation fraction and unconverted tail oil, wherein the unconverted tail oil circularly returns the solvent deasphalting device; and the lightweight distillation fraction and the DAO are mixed and enter the hydrogenation device of the boiling bed. The combined process course organically combines a decarbonization process and a hydrogenation process; and according to different properties of raw materials, a corresponding process and operation condition is adopted so as to maximize conversion of the residual oil material while minimizing equipment investment.

The invention relates to biomass poly-generation equipment and method for integral pyrolysis-flue gas combined cycle. The biomass poly-generation equipment comprises a pretreatment system, a drying system, a temperature regulation system, an integral pyrolysis furnace, a comprehensive combustion furnace, a fuel gas purification system, a carbon forming system, a gas storage cabinet and a solar collector. In order to solve the problems that the controllability of three processes, namely pyrolysis-pyrolysis gas cracking-solid carbon decoking in the prior art is weak and the integrity is insufficient, the invention provides the biomass poly-generation equipment and method for integral pyrolysis, the three heat absorption processes, namely pyrolysis, pyrolysis gas cracking and solid carbon decoking are completed in regions and segments in the same high temperature environment; the pyrolysis-pyrolysis gas cracking-solid carbon decoking functions are integrated and integral, the reaction process is controllable, fuel gas with a high heat value and such products as high temperature carbon, wood tar, wood vinegar are produced continuously and efficiently. The biomass is fully cracked and the product quality is effectively controlled.

The invention provides a method for preparing liquid alkane fuel by upgrading bio-oil in an aqueous phase catalytic mode. The method comprises the following steps of: 1) pretreating the bio-oil to obtain a water-soluble component and a water-insoluble component; 2) performing a pressurized acid hydrolysis process on a furan compound of the water-insoluble component to prepare the furan compound; 3) performing a reforming and hydrogen production reaction on the water-soluble component; 4) mixing the furan compound with a liquid-phase product separated from the step 3) to perform an aldol condensation reaction to increase carbon chains; and 5) performing a hydrogenation and dehydration reaction on an aldol condensation product to obtain liquid linear alkane. The method has the advantages that: an upgrading process, which is performed in a double-phase system, can effectively contribute to the desorption of an intermediate product from the surface of a catalyst and the mass transfer of an upgraded product, and can reduce the risk of carbon deposition on the surface of the catalyst; the quality of oil obtained by the method is high; the energy density and the energy grade of the bio-oil are improved greatly; and the liquid alkane fuel can be obtained from all kinds of bio-oil so as to partially substitute for the conventional widely-used fossil gasoline and diesel oil fuel.

The invention relates to an ignition device for a biomass gasification furnace and a using method thereof. In the device, an ignition bar formed by a heating wire and a ceramic tube element is vertically arranged in a three-way inlet tube of the biomass gasification furnace; the upper end of the ceramic tube element wound with the heating wire is positioned above a grate; the biomass gasificationfurnace are filled by granular biomass materials and compacted; the biomass materials are closely contacted with the heating wires; after the ignition bar is electrified, the biomass materials at theperiphery of the ignition bar is directly heated; a draught fan is opened after 10 to 20 seconds of heating, air is introduced to the bottom of the gasification furnace from the lateral side of the upper section of the ignition bar; the power supply of the ignition bar is closed after the electrification lasts for 10 to 20 seconds; and the ignition bar is twitched downwards and is rotated to ensure that the ignition bar is retracted inside the three-way inlet tube, the ignition bar is separated from the biomass material subjected to high-temperature gasification reaction with the ignition bar, and the air is introduced into the biomass gasification furnace from clearance between the upper end of the ignition bar and the inlet tube to maintain constant performance of the gasification reaction. The ignition device has the advantages of high success rate of ignition, short ignition time, simple and convenient operation and safe use.

A cracking furnace for the crack reaction of petroleum hydrocarbon features that its radiating segment includes n radiating regions isolated by furnace walls, which use a common convection segment, and the bottom burners are uniformly arranged at both sides of furnace wall. Its advantages are uniform heating, high heat transfer efficiency, and high productivity.

A composite catalyst for biological diesel-oil by high-acidity grease is carried out by mixing methyl sulfonic acid with tin tetrachloride and concentrated sulfuric acid in proportion of 1:1:1, and esterification reacting by composite catalyst 2.5-3% at 58-63 degree for 3.5-4 hrs to convert waste grease into biological diesel-oil. It's fast, has gentle reactive condition, higher recovery rate and better quality.

The invention relates to a method for producing functional grease containing rich phytosterin ester from high-acid-value vegetable oil. The method is characterized by comprising the following steps: (1) addition of reaction raw materials: adding phytosterin, high-acid-value grease and molecular sieve into a reaction kettle, adding 100-200ppm of antioxidant, heating to 45-60 DEG C, stirring and carrying out ultrasonic treatment to obtain a premixture, wherein the mole ratio of the phytosterin to free fatty acids in the high-acid-value grease is 1:1-5:1; (2) enzymatic ester exchange reaction: adding 5-40 g / L lipase into the premixture, and stirring to react at 45-60 DEG C under normal pressure for 6-12 hours; and (3) carrying out after-treatment on the product to obtain the functional grease containing rich phytosterin ester. The method can obviously lower the acid value of the high-acid-value vegetable oil and generate the new functional active component phytosterin ester, and the product is simple for separation and purification; and thus, the method can easily implement large-scale amplification.