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Hydrodesulfurization catalyst for removing sulfur compounds in medium/low-temperature coal tar and application thereof

A low-temperature coal tar, hydrodesulfurization technology, applied in physical/chemical process catalysts, molecular sieve catalysts, chemical/physical processes, etc., can solve the problems of reactor blockage, low cetane number, catalyst deactivation, etc., and achieve good Water resistance, good hydrodenitrogenation performance, high mechanical strength effect

Inactive Publication Date: 2012-09-26
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with petroleum secondary processing distillate oil hydrotreating catalysts, coal tar hydrogenation catalysts face several problems: first, the oxygen content is high, and the water produced by deoxidation will have an adverse effect on the catalyst activity, stability and strength; Second, the high content of colloid and carbon residue is likely to promote carbon deposition on the catalyst, resulting in catalyst deactivation and reactor blockage; third, high sulfur and nitrogen content in coal tar; fourth, coal tar contains a large amount of aromatics, which makes the diesel fraction ten The hexane number is very low, requiring deep dearomatization to make it saturated and open the ring, and strive to maximize the cetane number, so the catalyst requires suitable acidity

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0021] Weigh 400g of alumina precursor pseudoboehmite, 50g of bentonite, 50g of Hβ molecular sieve and BF 3 25 g and mix well, then add to the above mixture with a pore volume of 0.2-0.4cm 3 100g of pseudo-boehmite / g, 16g of squash gum, 48g of nitric acid, and 440g of distilled water were kneaded in a kneader for 55min, and then put into an extruder to extrude. The formed carrier was dried at 40°C for 4 hours, and then dried at 100°C for 10 hours, then heated to 650°C at a heating rate of 2°C / min, and fired for 8 hours to obtain 627g of the finished carrier. Calculated on a dry basis, alumina accounted for 80% of the total mass of the carrier, and silicon Aluminum acid accounts for 10% of the total mass of the carrier, and Hβ molecular sieve accounts for 10% of the total mass of the carrier.

[0022] Add 297g of ammonium metatungstate, 323g of nickel nitrate, and 289g of ammonium molybdate into 625g of distilled water, stir at 60°C to dissolve completely, then add 83g of phos...

Embodiment 2

[0026] Weigh 800g of alumina precursor pseudoboehmite, 86g of bentonite, 125g of Hβ molecular sieve and BF 3 55g and mix well, then add to the above mixture with a pore volume of 0.2-0.4cm 3 70g of pseudo-boehmite / g, 14g of squash gum, 30g of citric acid, and 923g of distilled water were kneaded in a kneader for 45min, and then put into an extruder to extrude. The formed carrier was dried at 25°C for 5 hours, and then dried at 100°C for 9 hours, then heated to 550°C at a heating rate of 2°C / min, and calcined for 6 hours to obtain 1026g of the finished carrier. Calculated on a dry basis, alumina accounted for 80% of the total mass of the carrier, silicon Aluminum acid accounts for 7% of the total mass of the carrier, and Hβ molecular sieve accounts for 13% of the total mass of the carrier.

[0027] Add 256g of ammonium metatungstate, 224g of nickel carbonate, and 205g of molybdenum trioxide into 600g of distilled water, stir at 40°C to dissolve completely, then add 60g of phos...

Embodiment 3

[0031] Weigh 1000g of alumina precursor pseudoboehmite, 103g of bentonite, 91g of Hβ molecular sieve and BF 3 80g and mix well, then add 0.2-0.4 cm pore volume to the above mixture 3 50g of pseudo-boehmite / g, 12g of squash gum, 28g of oxalic acid, and 858g of distilled water were kneaded in a kneader for 60min, and then put into an extruder to extrude. The formed carrier was dried at 15°C for 6 hours, and then dried at 100°C for 8 hours, then heated to 450°C at a heating rate of 5°C / min, and calcined for 6 hours to obtain 895 g of the finished carrier. Calculated on a dry basis, alumina accounted for 85% of the total mass of the carrier, silicon Aluminum acid accounts for 5% of the total mass of the carrier, and Hβ molecular sieve accounts for 10% of the total mass of the carrier.

[0032] Add 257g of ammonium paratungstate, 241g of nickel citrate, and 152g of molybdenum nitrate into 787g of distilled water, stir at 15°C to dissolve completely, then add 80g of phosphoric acid...

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Abstract

The invention discloses a hydrodesulfurization catalyst for removing sulfur compounds in medium/low-temperature coal tar and an application thereof, belongs to the technical field of hydrodesulfurization catalysts for coal tar, and aims to provide a catalyst which can deeply remove the sulfur compounds in the coal tar and has relatively high denitrification capacity, relatively high mechanical strength, relatively high water resistance, a certain specific surface area, proper pore volume and proper pore diameter. The technical scheme is as follows: the catalyst consists of an active ingredient, a carrier and an aid, wherein the carrier accounts for 60 to 75 percent of the total weight of the catalyst; the active ingredient accounts for 18 to 26 percent of the total weight of the catalyst; the aid accounts for 7 to 14 percent of the total weight of the catalyst; the active ingredient consists of metal tungsten, nickel and molybdenum; and based on metal oxides for calculation, tungsten trioxide accounts for 12 to 16 percent of the total weight of the catalyst; nickel oxide accounts for 5 to 7 percent of the total weight of the catalyst; and molybdenum trioxide accounts for 2 to 5 percent of the total weight of the catalyst.

Description

technical field [0001] The invention discloses a hydrodesulfurization catalyst for removing sulfur-containing compounds in medium-low temperature coal tar and an application thereof, belonging to the technical field of coal tar hydrodesulfurization catalysts. Background technique [0002] With the rapid development of the world economy and China's economy, the oil resources used as fuel are becoming less and less, resulting in high oil prices, which provides a golden development opportunity for the coal chemical industry, which has been at a disadvantage for a long time. my country is rich in coal resources, and coal tar is a by-product of coking, coal gasification, and coal chemical industries. With the development of the coal chemical industry, its output is increasing year by year. At present, the annual output of coal tar is about 15 million tons, of which the annual output of high-temperature coal tar is about 10 million tons, and the annual output of medium-low tempera...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/78C10G45/08
Inventor 赵敏邱泽刚武行洁
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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