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A Catalytic Process for Tire Cracking Oil Distillate Fixed Bed Hydrogenation and Upgrading

A tire pyrolysis oil, hydrogenation modification technology, applied in the direction of hydrogenation treatment process, petroleum industry, hydrogenation refining of aromatic hydrocarbons, etc., can solve the problems of unfavorable miniaturization operation production, complicated process flow, large investment, etc., and achieve the product Obvious modification effect, great economic benefit and environmental benefit, effect of content reduction

Active Publication Date: 2019-11-05
浙江绿保再生资源科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This requires the construction of multiple sets of equipment, the overall process is more complicated, and the investment is large, which is not conducive to small-scale production

Method used

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  • A Catalytic Process for Tire Cracking Oil Distillate Fixed Bed Hydrogenation and Upgrading
  • A Catalytic Process for Tire Cracking Oil Distillate Fixed Bed Hydrogenation and Upgrading
  • A Catalytic Process for Tire Cracking Oil Distillate Fixed Bed Hydrogenation and Upgrading

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Embodiment 1

[0032] A tire cracking oil distillate fixed bed hydrogenation upgrading catalytic process, including a reaction device for upgrading raw material oil formed by connecting the first, second and third reactors in series, and the raw material oil is gasoline of tire cracking oil When with the stock oil A of the diesel fraction, the gasoline and diesel mass ratio in the stock oil A is 1:(1.5-4.5), and the gasoline and the diesel mass ratio in the stock oil A of the present invention are preferably 1:2. The inner diameter of the first, second and third reactors is 24mm, the height is 1380mm, the outer diameter of the thermocouple casing is 9.5mm, and the average cross-sectional area of ​​the reactor is 381.5mm 2 , the first, second and third reactors are continuously heated by 5 furnace tiles installed in the heater, each furnace tile is 23cm high, and the total height is 115cm. The distance between the reactor inlet and the first furnace tile is 10cm, and the fifth furnace tile Th...

Embodiment 2

[0042] A tire cracking oil distillate fixed bed hydrogenation upgrading catalytic process, including a reaction device for upgrading raw material oil formed by connecting the first, second and third reactors in series, and the raw material oil is gasoline of tire cracking oil , diesel oil and the stock oil B of wax oil fraction, the mass ratio of the gasoline in stock oil B, diesel oil and wax oil is 1:(1.5-3.5):(1.5-3.5), in the stock oil B of the preferred present invention The mass ratio of gasoline, diesel and wax oil is 1:2:1.8. The inner diameter of the first, second and third reactors is 26mm, the height is 1380mm, the outer diameter of the thermocouple casing is 9.5mm, and the average cross-sectional area of ​​the reactor is 381.5mm 2 , the first, second and third reactors are continuously heated by 5 furnace tiles installed in the heater, each furnace tile is 23cm high, and the total height is 115cm. The distance between the reactor inlet and the first furnace tile is...

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Abstract

The invention belongs to the technical field of petroleum chemical industry, and particularly relates to a tire pyrolysis oil fraction fixed bed hydro-upgrading catalysis process. The process includes a reaction device formed by serially connecting first, second and third reactors and used for upgrading of raw material oil. The process has the advantages that gasoline-diesel products higher in added value can be produced after fractionation, so that utilization value of tire pyrolysis oil is increased obviously, and bigger economic benefit and environmental benefit in the process of tire pyrolysis are realized; the process is simple in procedure, low in investment cost and conducive to realizing small-scale production.

Description

technical field [0001] The invention belongs to the technical field of petrochemical industry, in particular to a fixed-bed hydrogenation and upgrading catalytic process for tire cracking oil fractions. Background technique [0002] With the continuous development of the automobile industry, the demand for rubber products such as tires is also increasing. At the same time, the generation of waste tires is also increasing sharply. In 2009, my country’s production of tires consumed rubber accounted for about 70% of the country’s total consumption of rubber resources, and the annual waste tires produced weighed about 8.6 million tons. If all of them can be recycled and reused, it is equivalent to my country’s 5-year natural rubber output. As of 2015, the production of waste tires in my country has reached 11 million tons. From the perspective of environmental protection and resource utilization maximization, compared with the current disposal methods of waste tires such as lan...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G65/02C10G45/08C10G45/50
CPCC10G45/08C10G45/50C10G65/02C10G2300/1037C10G2300/202C10G2300/70C10G2400/04
Inventor 朱爱林李呈宏罗明生
Owner 浙江绿保再生资源科技有限公司
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