Method for preparing direct reduced iron by bio-oil
A technology of bio-oil and reduced iron, which is applied in chemical instruments and methods, inorganic chemistry, furnace types, etc., can solve the problems of undiscovered bio-oil application, supply, price and regional restrictions, and achieve abundant stocks and be conducive to environmental protection , easy-to-operate effect
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Embodiment 1
[0022] This example examines the effect of using the method of the present invention to prepare direct reduced iron using bio-oil and hematite powder obtained from rapid pyrolysis of sawdust as raw materials.
[0023]The electrocatalytic steam reforming bio-oil hydrogen production reactor in the prior art (ZL 200710134707.1) is used as the reaction device prepared from bio-oil. The method of preparing reduced synthesis gas from bio-oil: First, the conventional commercial Ni-based catalyst is reduced in a hydrogen atmosphere at 500°C for one hour, and then filled around the built-in electric furnace wire and evenly contacted with the surface of the electric furnace wire, the amount of catalyst is determined by bio-oil per hour The amount of feed is determined. In this embodiment, the amount of catalyst used is 5.5g, and then the power supply of the electric heating belt in the preheating zone is turned on, so that the temperature in the preheating zone is 180-200 ° C; the Ni-Cr ...
Embodiment 2
[0031] This example mainly investigates the effect of using the method of the present invention to prepare direct reduced iron using bio-oil obtained from rapid cracking of rice husk and limonite powder as raw materials.
[0032] In this embodiment, the reaction device and the method for the reduction of synthesis gas from bio-oil and the reduction of iron ore are the same as in Example 1, except that the bio-oil and limonite powder obtained by rapid cracking of rice husk are When making direct reduced iron from raw materials, when the reaction temperature of bio-oil reforming is 548°C, the current is 2.9A, the flow rate of water vapor is 50g / h, the flow rate of bio-oil is 18g / h, and the corresponding molar ratio of water vapor and bio-oil is 7 , the hydrogen production rate and bio-oil conversion rate were 93.5% and 95.1%, respectively, and the cooled mixed gas included hydrogen (69.3vol%), carbon dioxide (24.8vol%), carbon monoxide (5.1vol%) and methane (0.2vol%) , using con...
Embodiment 3
[0036] This example mainly investigates the effect of using the method of the present invention to prepare direct reduced iron by using bio-oil and magnetite powder obtained by rapid pyrolysis of sawdust as raw materials.
[0037] In this example, the reaction device and method for reducing syngas from bio-oil and iron ore reduction are the same as in Example 1. When the bio-oil reforming reaction temperature is 555°C, the current is 3.1A, When the flow rate is 50g / h, the bio-oil flow rate is 18g / h, and the molar ratio of water vapor and bio-oil is 7, the hydrogen production rate and bio-oil conversion rate are 97.2% and 98.9% respectively, and the mixed gas after cooling includes hydrogen (70.8vol%), carbon dioxide (25.5vol%), carbon monoxide (3.5vol%) and methane (0.1vol%), use conventional chemical absorption method (20%NaOH solution) to eliminate carbon dioxide in the mixed gas, and obtain hydrogen containing 93.1vol% and high-grade reducing gas of 4.5vol% carbon monoxide,...
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Abstract
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