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Thermally dissolving and catalytic method for preparing liquid fuel by lignite as well as catalyst and solvent used therefor

A liquid fuel and catalyst technology, applied in the field of catalysts and solvents, can solve the problems of high technical requirements, harsh conditions and large investment, and achieve the effects of simple preparation equipment, mild operating conditions and low investment

Active Publication Date: 2008-05-21
ZHAOQING SHUNXIN COAL CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process is relatively mature, but its disadvantages are: the conversion rate of organic matter is low, and the pollution in the processing process is large; (2) Indirect coal liquefaction method: the basic process of this process is to first gasify coal into synthesis gas (CO and H 2 ), under the catalysis of iron agent, cobalt agent and ruthenium agent, liquid fuel is prepared by Fischer-Tropsch reaction (Fischer-Tropsch Reaction)
However, the disadvantages of this process are: complex process, large investment, high cost, and high technical requirements; (3) high-pressure hydrogenation liquefaction method of coal: the process is characterized by high pressure (10-30MPa), high temperature (450-500°C ) and catalysts, the polymer chemical structure of coal is destroyed and hydrogenated
However, the disadvantages of this process are: harsh conditions, high requirements for equipment, large investment and high cost
The process is simple, but the oil yield is very low, and its products cannot be used directly, and must be compounded with kerosene or methanol, so it is called substitute diesel oil

Method used

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  • Thermally dissolving and catalytic method for preparing liquid fuel by lignite as well as catalyst and solvent used therefor

Examples

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preparation example Construction

[0030] The preparation method of the circulating solvent is as follows: take part of the liquid product separated from step 4), and undergo two-stage hydrogenation, the first-stage hydrogenation temperature is 280-350°C, the second-stage hydrogenation temperature is 310-390°C, and the pressure is 6-13MPa. Hydrogen oil ratio 300~500(v / v), space velocity 0.2~1.2h -1 Under certain conditions, the solvent obtained is suitably hydrogenated. If the obtained solvent meets the following indicators: density 0.96~0.98g / l, distillation range 200~400°C, hydrogen content (m%) 7.6%~10%, then enter the step 2) coal slurry of the above method as a circulating solvent instead of anthracene oil In preparation; if the above indicators are not met, return to the circulating solvent preparation process for rehydrogenation. The catalysts required for the preparation of circulating solvents are general industrial oil hydrogenation catalysts such as the hydrogenation refining catalysts FRIPP3926 and...

Embodiment 1~7

[0050] Put the pulverized and dried coal powder (80-200 mesh in particle size, 2%-5% moisture) and the circulating solvent generated by the method itself into the coal slurry tank according to the ratio required by the method and a certain amount of catalyst. The coal slurry used in the method is prepared through thorough stirring and mixing in the slurry preparation tank. The coal slurry is sent to the hot-melt catalytic reactor, and the reaction is carried out under the liquefaction condition of the method. The reaction material from the reactor enters the separation device, and the three-phase material of gas, liquid and solid is separated. The gas is treated to meet the environmental protection requirements and enters the heating system as fuel gas; the solid is used as liquefied residue and enters the residue treatment system; liquid material Part of it enters the circulating solvent preparation device, and part of the circulating solvent required by the production method...

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Abstract

The invention belongs to the technological field of coal chemical processing and discloses a heat dissolving and catalyzing method using brown coal to prepare liquid fuel. The method comprises the following steps: 1) the brown coal is smashed and dried to prepare pulverized coal; 2) the pulverized coal, solvent and catalyst are stirred and mixed well to prepare coal slurry; wherein, the weight percent of the pulverized coal is 30 percent to 40 percent; the weight percent of the solvent is 60 percent to 70 percent; the quantity of the added catalyst is 0.5 percent to 1 percent of the weight of the pulverized coal; 3) the coal slurry is dissolved by heat and catalyzed to prepare heat dissolved and liquefied products; wherein, the temperature is 390 DEG C to 450 DEG C; the pressure is 5.0MPa to 9.0MPa; the reaction time is 30 minutes to 60 minutes; 4) the heat dissolved and liquefied products are separated to form gas-phase, liquid-phase and solid-phase products; 5) the liquid products are extracted and processed to form liquid fuel. The invention also discloses catalyst and solvent used in the method. The operation condition of the method of the invention is mild; the conversion ratio of the organic substances in the brown coal can achieve a higher level; after being processed, the liquid fuel product can be used for preparing engine fuel suiting national standards; and the preparation equipment is simple; the investment is small; the cost is low; and the invention is a coal liquefaction method suiting the national conditions of China.

Description

technical field [0001] The invention belongs to the technical field of coal chemical processing, and in particular relates to a hot-melt catalytic method for preparing liquid fuel from lignite and the catalyst and solvent used therein. Background technique [0002] At present, there are three main methods of producing liquid fuel from coal, which are summarized by domestic and foreign data: (1) pyrolysis of coal (low temperature, high temperature dry distillation): the basic process of this process is to put coal under the action of heat Decomposition and polymerization are generally carried out at normal pressure and above 400°C to obtain hydrogen-rich gas, low molecular liquid tar and coke. This process is relatively mature, but its disadvantages are: the conversion rate of organic matter is low, and the pollution in the processing process is large; (2) Indirect coal liquefaction method: the basic process of this process is to first gasify coal into synthesis gas (CO and H...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G1/06B01J31/16B01J31/04
CPCB01J31/146B01J31/1805C01G39/00C01G1/06C01G51/00B01J31/2213B01J2531/845B01J2531/37C01G49/00B01J2531/64B01J2531/842C01G29/00
Inventor 吴克陈翀黄文益彭派吴春来
Owner ZHAOQING SHUNXIN COAL CHEM TECH
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