High Temperature Coal Tar Distillate Hydrogenation Unit with Low Aromatic Oil Recycle

A technology of high-temperature coal tar and distillate oil, applied in the field of coal chemical industry, can solve the problems of difficult control of hydrofining reactor temperature, high asphalt content, coking of catalyst, etc., and achieve reasonable structure, easy reaction temperature, and moderate reaction heat release Effect

Active Publication Date: 2017-06-20
NINGBO RES & DESIGN INST OF CHEM IND
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  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process of processing high-temperature coal tar, due to the high content of high-temperature coal tar pitch, it is easy to cause coking of the catalyst in the hydrotreating reactor; Vigorous, making it difficult to control the temperature of the hydrofining reactor and difficult to operate

Method used

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  • High Temperature Coal Tar Distillate Hydrogenation Unit with Low Aromatic Oil Recycle

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Embodiment Construction

[0015] The present invention will be further described in detail below in conjunction with the accompanying drawings and embodiments.

[0016] Such as figure 1 As shown, the high-temperature coal tar distillate hydrogenation unit with low-aromatic oil circulation in this embodiment includes a vacuum distillation tower 1, a hydrotreating reactor 2, a separation system 3, a desulfurization tower 4, a fractionation tower 5 and a hydrogenation A cracking reactor 6, the middle part of the vacuum distillation tower 1 is provided with a high-temperature coal tar inlet, the bottom of the vacuum distillation tower 1 is provided with a heavy fraction outlet, and the top of the vacuum distillation tower 1 is provided with a light fraction outlet. The top of the hydrofinishing reactor 2 is provided with a reaction feed port, and the reaction feed port is connected with the light fraction outlet of the vacuum distillation tower 1, and the bottom of the hydrofinishing reactor 2 is provided ...

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Abstract

The invention discloses a high-temperature coal tar distillate oil hydrogenation device with low aromatic oil circulation. The high-temperature coal tar distillate oil hydrogenation device comprises a vacuum distillation tower, a hydrorefining reactor, a separation system, a desulfurizing tower, a fractionating tower and a hydrocracking reactor, wherein a high-temperature coal tar inlet is formed in the vacuum distillation tower; a heavy distillate outlet is formed in the bottom of the vacuum distillation tower; a light distillate outlet is formed in the top of the vacuum distillation tower; a reaction feeding hole connected with the light distillate outlet is formed in the top of the hydrorefining reactor; a discharge hole is formed in the bottom of the hydrorefining reactor and is connected with the separation system; a hydrogen outlet is formed in the top of the separation system; a liquid-phase outlet is formed in the bottom of the separation system and is connected with the desulfurizing tower; a liquid-phase outlet connected with the fractionating tower is formed in the bottom of the desulfurizing tower; a distillate outlet is formed in the fractionating tower; one part of distillate which is greater than 350 DEG C is fed to the hydrocracking reactor as untransformed oil; the other part is mixed with light distillate as low aromatic oil and is fed to the hydrorefining reactor; a feeding hole is formed in the top of the hydrocracking reactor; and an outlet connected with the separation system is formed in the bottom of the hydrocracking reactor. The high-temperature coal tar distillate oil hydrogenation device has the characteristics of being reasonable in structure, and simple to operate, and the reaction temperature is easy to control.

Description

technical field [0001] The invention belongs to the technical field of coal chemical industry, and in particular relates to a high-temperature coal tar distillate oil hydrogenation device with low-aromatic oil circulation. Background technique [0002] Coal tar is one of the important by-products of coal coking and occupies a certain share in the production of coal coke. Based on the current coal coking technology, coal tar production accounts for about 3.5% to 4.2%. However, due to the constraints of backward technology in the downstream chemical industry, the huge amount of coking by-products of coal tar is difficult to use with high added value. At present, the consumption market of high-temperature coal tar in my country is mainly divided into three parts, one is to use crude coal tar as a fuel to replace heavy oil, to use it in thermal energy industries such as glass and ceramics, and as a raw material for producing carbon black; the other is to export it; the third is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G67/00
CPCC10G67/00
Inventor 项文裕项裕桥谢琤
Owner NINGBO RES & DESIGN INST OF CHEM IND
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