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Heterogeneous coal tar suspension bed hydrogenation method

A coal tar and suspended bed technology, applied in the field of coal chemical industry, can solve the problems of inflexible cutting method, no coal tar raw material utilization, inability to transport, etc., achieve flexible and optimized plan, improve cetane number, and save processing steps Effect

Active Publication Date: 2013-08-28
CCTEG CHINA COAL RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The disadvantage of these methods is that the coal tar raw material is not fully utilized
[0008] The authorized patent CN101885982A that the applicant applied for earlier provides the coal tar suspension bed hydrogenation method of the heterogeneous catalyst that makes the coal tar raw material produce light oil in a large amount, greatly improves the utilization rate of the raw material and the efficiency of the catalyst, but, During the actual use of this patent, the applicant found that when the source process of the coal tar raw material is different, the coal tar raw material needs to be pretreated to meet the production needs, and the cutting method of the patent CN101885982A is obviously not flexible enough, especially when When the viscosity of the pretreatment object is high, there will be phenomena such as failure to convey

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  • Heterogeneous coal tar suspension bed hydrogenation method
  • Heterogeneous coal tar suspension bed hydrogenation method
  • Heterogeneous coal tar suspension bed hydrogenation method

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] A typical coal tar is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 1:

[0038] Table 1 Properties of Coal Tar Raw Materials

[0039]

[0040]

[0041] The pretreated coal tar is distilled and separated into IBP~260℃, 260~350℃ and heavy fractions greater than 350℃, and the heavy fraction oil greater than 350℃ is used as the raw material oil of the suspension bed hydrogenation reactor for hydrocracking light reaction.

[0042] The catalyst used in this example is a molybdenum-iron composite suspension bed hydrogenation catalyst, and the catalyst used includes molybdenum with a high activity metal component and iron with a low activity metal component, wherein the metal molybdenum with a high activity component and the iron metal with a low activity component The weight ratio is 1:500, the water content of the catalyst is l...

Embodiment 2

[0053] A kind of coal tar with higher heavy fraction content is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 4: the heavy fraction content of this feedstock oil is high, and the viscosity Higher, the viscosity at 40 ° C is more than 17 times that of the raw material oil in Example 1. Considering the problem of industrial equipment transportation, the viscosity of the material is too high to realize transportation. The raw material pretreatment is that the cutting temperature of distillation and separation of heavy distillate oil should be at 310°C.

[0054] Table 4 Properties of Coal Tar Raw Materials

[0055]

[0056]

[0057] In this experiment, the pretreated coal tar was separated into IBP~310°C and greater than 310°C heavy fractions by distillation, and the heavy fractions greater than 310°C were used as the feedstock oil o...

Embodiment 3

[0067]A kind of coal tar with higher heavy fraction content is selected as the coal tar raw material of this example, and the properties of the coal tar raw material after conventional dehydration and mechanical impurity pretreatment are shown in Table 7: the heavy fraction content of this raw material oil is high, and the viscosity Higher, the viscosity at 40 ° C is more than 17 times that of the raw material oil in Example 1. Considering the problem of industrial equipment transportation, the viscosity of the material is too high to realize transportation. The raw material pretreatment is that the cutting temperature of distillation and separation of heavy distillate oil should be at 280°C.

[0068] Table 7 Properties of Coal Tar Raw Materials

[0069]

[0070] In this experiment, the pretreated coal tar was separated into IBP~280°C and greater than 280°C heavy fractions by distillation, and the heavy fractions greater than 280°C were used as feedstock oil for the suspens...

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Abstract

The invention discloses a heterogeneous coal tar suspension bed hydrogenation method which comprises the following steps: mixing catalyst oil slurry with full fraction or heavy fraction oil of coal tar and catalyst-containing circulating oil, adding into a suspension bed hydrogenation reactor, and performing hydrocracking reaction, wherein the catalyst is a powdery particle coal tar suspension bed hydrogenation catalyst containing a single-metal active component or composite multi-metal active component of molybdenum, nickel, cobalt, tungsten or iron; separating out light oil from the hydrogenation reaction product, and then directly circulating a large amount of the tail oil containing the catalyst to the suspension bed reactor; and performing catalyst removal treatment on a small amount of the tail oil, recirculating to the suspension bed reactor, and performing further light fraction conversion. The heavy oil is wholly or maximally circulated to realize the maximal, convenient and flexible light oil production from the coal tar having different characteristics and the cyclic utilization of the catalyst, thus greatly improving the utilization efficiency and operating flexibility of the raw materials and the catalyst.

Description

technical field [0001] The invention belongs to the field of coal chemical industry, and in particular relates to a heterogeneous coal tar suspended bed hydrogenation method for maximum production of engine fuel and chemical raw materials by using coal tar as a raw material. Background technique [0002] Coal tar is an important by-product in the coal pyrolysis and carbonization process. It is a complex mixture. According to the temperature and process of coal pyrolysis and carbonization, coal tar can be divided into low-temperature coal tar, medium-temperature coal tar and high-temperature coal tar. , and their compositions vary greatly. [0003] At present, the conventional processing process of coal tar in my country is to cut various fractions concentrated in components through pretreatment distillation, and then use physical or chemical methods (such as acid-base washing, distillation, polymerization, crystallization methods) to process various fractions to extract vari...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C10G47/26
CPCC10G3/00C10G47/26C10G2300/44C10G2300/80Y02P30/20
Inventor 张晓静李培霖毛学锋王勇王雨胡发亭石智杰颜丙锋黄澎赵渊杜淑凤谷小会朱肖曼吴艳赵鹏张帆马炳辰周铭钟金龙孙竟晔李伟林陈来夫常秋连
Owner CCTEG CHINA COAL RES INST
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