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Hydrogenation reaction device

A technology of hydrogenation reaction and hydrogenation reactor, which is applied in the preparation of amino compounds, organic compounds, organic chemistry, etc. It can solve the problems of too large stirring motor of the reactor, frequent mechanical failures, and reduce the reaction volume, etc., to achieve Compact structure, small thermal resistance of dirt, and reduced reaction volume

Active Publication Date: 2013-07-31
甘肃银光聚银化工有限公司 +1
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  • Claims
  • Application Information

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Problems solved by technology

The DNT hydrogenation reaction rate is greatly affected by the DNT concentration. It is a 0-order reaction in the high-concentration area (≥600PPm), and a 1-order reaction in the low-concentration area (≤600PPm). According to the principle of reaction kinetics, the two-stage series can be greatly improved. The reaction driving force of the reactor is improved, the reaction volume is reduced, and the reaction efficiency is improved. Therefore, the present invention adds protection to the reactor. Through the operation of two kettles in series, the reaction volume is greatly reduced, and the excessive stirring motor of the reactor and the production energy consumption are solved. High, frequent mechanical failures and other issues

Method used

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Embodiment Construction

[0046] The following examples serve to further illustrate the method of the present invention. The spirit and scope of the present invention disclosed above are not limited by these examples. Those skilled in the art will readily appreciate that known variations can be made using the conditions of the following methods.

[0047] preferred embodiment

[0048] Hydrogenation reactor:

[0049] ①Body: Due to high-pressure equipment, an elliptical head is selected, with a diameter of φ2400mm, a barrel height of 3700mm, a head height of 600mm, a total equipment height of 4900mm, a straight edge height of 50mm, and a head volume of 2.05m 3 , with a height of 4.20mm and a total volume of 18.32m 3 , the effective volume is 14.879m 3 . Shaft sleeve 220mm×4mm, shaft φ110mm / φ60mm, cooling water main inlet pipe φ210mm×5mm, 4 pieces. The lower manhole is φ750mm, and the discharge pipe is φ230mm×40mm.

[0050] ②Plate cooler: curved plate, width 940mm, height 2500mm, thickness 14mm, arc l...

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Abstract

The invention relates to a high-efficiency hydrogenation device and a dinitrotoluene hydrogenating method. Three hydrogenation reactors are connected in parallel and are all connected with a hydrogenation aging machine in series; the bottom part of an inclined grid plate separator (7) is connected with the bottom parts of the three hydrogenation reactors in parallel, and the top part of the inclined grid plate separator (7) is connected with a steam-liquid separator tank which is connected with inclined grid plate separators (8) and (9) in parallel; the top parts of the inclined grid plate separators are connected with a tolylenediamine finished product tank in parallel, and the bottom parts of the inclined grid plate separators are connected with a catalyst recovery tank in parallel; andthe bottom part of the catalyst recovery tank is connected with the top parts of the three hydrogenation reactors in parallel through a diaphragm pump. In the invention, the size of the hydrogenationreactors are reduced considerably, the power of a stirring motor is lowered, and the energy conservation and consumption reduction of the device are realized.

Description

technical field [0001] The invention relates to a gas-liquid-solid three-phase hydrogenation reaction device for preparing toluenediamine (TDA) by hydrogenation reaction of dinitrotoluene (abbreviated as DNT). Background technique [0002] Hydrogenation reaction is an important step in the three core reactions of nitration, hydrogenation and photochemical production in TDI production, and is one of the key technologies in TDI production. Hydrogenation reactor is the core production equipment of hydrogenation reaction, and its technological advancement directly affects TDI The level of production cost and the process stability of the whole production line. [0003] The hydrogenation reaction equation of dinitrotoluene hydrogenation to generate toluenediamine is as follows: [0004] [0005] The hydrogenation reaction is a reaction with a large heat release, and the reaction heat must be transferred in time, so there is a cooler with a large heat transfer surface in the re...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J8/10C07C211/51C07C209/36
Inventor 尹世英李晓明沈精平李明郑继祥汤汉球赖大忠强光明谢小刚梁文贵马玉靖耿天奇李虎邦蒙鸿飞胡安魁
Owner 甘肃银光聚银化工有限公司
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