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Driving inlet method of aniline liquid phase hydrogenation reactor

A reactor and aniline liquid technology, which is applied in the field of liquid-phase hydrogenation reactors of aniline devices, can solve the problems affecting the service life of the reactor, the distortion and extrusion of the tray, and the damage of the internal parts of the reactor, and achieves easy operation and reduced reduction. The effect of minor maintenance frequency and prolonging service life

Active Publication Date: 2010-02-17
TIANJI COAL CHEM IND GROUP
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AI Technical Summary

Problems solved by technology

When bleed air, when the cut-off valve on the main line of hydrogen into the reactor is opened, the accumulated hydrogen can easily allow the air flow to carry the material at the bottom of the reactor to impact the internals of the reactor tray, causing serious damage to the internals of the reactor, especially the tray Severely distorted, squeezed and deformed, the reactor had to be shut down for maintenance, which not only caused serious economic losses, but also greatly affected the service life of the reactor, and also brought great hidden dangers to safe production

Method used

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  • Driving inlet method of aniline liquid phase hydrogenation reactor
  • Driving inlet method of aniline liquid phase hydrogenation reactor

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Embodiment Construction

[0010] Such as figure 2 As shown, a bypass line 3 (2″) is newly added at the shut-off valve 2 on the hydrogen main line (10″), and a bypass valve 4 is installed on the bypass line 3, and the original DCS in the central control room The hydrogen pressure signals PT and PT are connected to the newly added pressure difference indicator signal PDI, so that the pressure difference on both sides of the shut-off valve 2 is indicated in the DCS, and the alarm (30KPa) and interlock (50KPa) parameters are set at the same time.

[0011] When the aniline liquid-phase hydrogenation reactor is started up, the bypass valve 4 installed on the bypass line 3 is first opened. After the hydrogen is pretreated, it first passes through the newly added bypass line 3, and then enters the reactor 1 through the distributor. When the differential pressure indicator signal PDI shows that the pressure difference between the upstream and downstream of the shut-off valve 2 is below 50KPa, then open the shu...

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Abstract

The invention relates to a driving inlet method of an aniline liquid phase hydrogenation reactor. An inlet reactor hydrogen main pipeline is connected at the bottom of the aniline liquid phase hydrogenation reactor, and a trip valve is arranged on the inlet reactor hydrogen main pipeline. The driving inlet method of the aniline liquid phase hydrogenation reactor is characterized in that the trip valve of the inlet reactor hydrogen main pipeline is provided with a pipeline, and a bypass valve is arranged on the bypass pipeline; the bypass valve arranged on the bypass pipeline is started firstly at the time of driving, when pressure at both sides of the trip valve is balanced, the trip valve is then started, and the bypass valve arranged on the bypass pipeline is closed after meeting the driving requirement of the reactor system. The inlet method can prevent the damage of the hydrogenation reactor on internal parts in the process of driving hydrogen introduction, prolong the service life of the reactor and reduce the repair frequency of the reactor.

Description

technical field [0001] The invention relates to a liquid-phase hydrogenation reactor of an aniline plant, in particular to a gas intake method in the start-up stage of the liquid-phase hydrogenation reactor of an aniline plant. Background technique [0002] The start-up process of the aniline liquid-phase hydrogenation reactor is relatively complicated. The key is to introduce hydrogen before feeding, until the hydrogen content of the reactor system and the reactor pressure meet the start-up requirements. Its process is as figure 1 , the bottom of the aniline liquid-phase hydrogenation reactor 1 is connected to the reactor hydrogen main line, and a cut-off valve 2 is installed on the reactor hydrogen main line. The system pressure required for the start-up of the aniline liquid-phase hydrogenation reactor is 1.7MPa (absolute pressure). Before start-up, the pressure in the reactor is normal pressure, and the pressure in the hydrogen pipeline network is 1.9MPa (absolute press...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C211/46C07C209/36
Inventor 沈凤林余海兵
Owner TIANJI COAL CHEM IND GROUP
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