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A kind of heavy tar selective catalytic upgrading device and method thereof

A heavy tar, selective technology, applied in chemical instruments and methods, tar processing, tar processing by heat treatment, etc., can solve inevitable problems, achieve improved tar yield, reduce dust content, improve tar quality effect

Active Publication Date: 2022-07-01
SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, in this method, heavy tar and light tar are all catalyzed, and light tar is inevitably converted into heavy part and pyrolysis gas, resulting in a decrease in tar yield.

Method used

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  • A kind of heavy tar selective catalytic upgrading device and method thereof
  • A kind of heavy tar selective catalytic upgrading device and method thereof

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Embodiment

[0030] like figure 1 As shown, a device for selective catalytic upgrading of tar includes an external heating furnace 1 and an internal reactor 2, the internal reactor 2 is provided with an internal member 2-2, and the internal member 2-2 is provided with a volatilization The pores or channels through which the fractions pass, so that pyrolysis produces radial flow of volatiles. A solid fuel channel 2-1 is formed between the inner member 2-2 and the outer wall of the reactor 2. A solid fuel feeding port is provided at the top of the solid fuel channel 2-1, and a slag discharge port is provided at the bottom of the solid fuel channel 2-1 for discharging heat. The semifocal formed by the solution. The solid fuel channel 2-1 is not provided with a gas outlet, so that the pyrolysis volatiles can only be discharged through the pores or pores on the inner member 2-2.

[0031] Inside the inner member 2-2 is a volatile channel 2-3. The volatile component channel 2-3 is divided into...

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Abstract

A heavy tar selective catalytic upgrading device and a method thereof, relate to a catalytic upgrading device and a method thereof, the device is divided into a heating zone and a reactor, the inner member of the reactor is arranged with pores or channels, and the solid The fuel is fed into the solid fuel channel from the top, and is pyrolyzed by the outer high temperature area. The pyrolysis products radially pass through the solid fuel bed at low temperature in the center, and the light tar and gas enter the light component channel directly from the upper region of the reactor. It is directly discharged from the reactor; as the bed moves down, the temperature of the central bed gradually increases, and the adsorbed heavy tar is desorbed again, enters the heavy tar channel, and then undergoes catalytic cracking and upgrading through the catalyst layer. Semi-coke produced by pyrolysis is discharged from the lower section of the reactor. The invention realizes the selective catalytic cracking of the heavy tar with poor quality, improves the tar quality, avoids the obvious decrease of the tar yield caused by the catalytic cracking of the light tar, and realizes the tar yield on the basis of minimizing the decrease of the tar yield. Quality improvement.

Description

technical field [0001] The invention relates to a tar catalytic cracking device and a method thereof, in particular to a heavy tar selective catalytic upgrading device and a method thereof. Background technique [0002] Hydrocarbon solid fuels include coal, biomass, oil shale, urban solid waste, etc. Currently, the main utilization methods are direct combustion and gasification, neither of which efficiently utilizes the high value-added volatiles in solid fuels. Through pyrolysis technology, hydrogen-rich volatiles can be precipitated in the form of high-quality liquid products and gas-phase products under mild conditions, and carbon-rich semi-coke can be obtained at the same time. Pyrolysis tar can extract high-value aromatic chemicals or hydrogenate to produce fuel oil, which can make up for the shortage of oil supply in my country to a certain extent. The pyrolysis gas has a high calorific value. Combustion to generate electricity for heating or to synthesize chemicals su...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/02C10C1/20C10C1/19
CPCB01J8/02B01J6/008B01J8/0278C10C1/19C10C1/20C10C1/205B01J2208/00017
Inventor 贾鑫许光文韩振南张玉辉宋兴飞
Owner SHENYANG INSTITUTE OF CHEMICAL TECHNOLOGY