Fixed bed composite reaction equipment

A combined reaction and fixed bed technology, applied in chemical/physical processes, chemical instruments and methods, etc., can solve problems such as increase, excessive heat transfer, increase heat transfer temperature difference and enhance heat transfer

Active Publication Date: 2009-07-15
杭州林达化工技术工程有限公司
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Aiming at this fundamental contradiction, the present invention breaks through the existing use of coolants at the same temperature, and uses coolants of different temperatures in different sections of the reactor to solve the problem, so that the heat exchange in the reaction can be designed according to the size of the reaction heat removed, which can be specifically determined according to the reaction The flow direction of the gas in the catalyst layer is sequentially divided into multiple blocks before and after, and the coolant is used to exchange heat indirectly through the heat exchange tube. For reactions such as methanol synthesis, where the reaction temperature is within the range of 180°C to 300°C, pressurized heating can be used. Water is used as the heat carrier, and the heat absorbed by the vaporization of the liquid in the reactor is much higher than the sensible heat absorbed by the temperature rise of the cooling medium. For a higher reaction temperature, mineral oil with low volatility, he

Method used

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Examples

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Embodiment 1

[0023] The combined reaction equipment of the present invention is used for methanol synthesis reaction, uses water as cooling medium, adopts figure 2 The reaction equipment is shown. figure 2 A solid valve means the valve is closed, and a hollow valve means the valve is open. The steam drum 51 is connected to the heat exchange block area 21 and can be vaporized at a low pressure of 0.5-3 MPa, and the steam drum 52 is connected to the heat exchange block areas 22 and 23 and can be vaporized at a pressure of 1-5 MPa. The reaction gas reacts from top to bottom in the catalytic reaction block areas 31, 32, and 33. The upper part has a high reaction speed and a large reaction heat, and can react at a temperature of 230-280 ° C. There is a heat transfer temperature difference of tens of degrees between the inside and outside of the heat exchange block area 21 , The heat transfer block area 22, 23 outer catalyst layer reaction heat is small, can react at 220~270 ℃, the heat trans...

Embodiment 2

[0028] Embodiment 2: generate phthalic anhydride (B) with air catalytic oxidation o-xylene (A), literature shows (Zhu Bingchen editor-in-chief, chemical reaction engineering, Chemical Industry Press, P167), " raw material gas is air and o-xylene Toluene mixture, wherein o-xylene is 0.8432%, oxygen 20.33%, nitrogen 78.8268% (volume ratio), the main reaction heat of generating product is 1285KJ / mol, and the production side reaction CO, CO 2 The heat of reaction is 4561KJ / mol, with V 2 o 5 Titanium compound is used as catalyst, operating pressure is 0.1275MPa, shell-and-tube reactor tube inner diameter is 26mm, tube length is 3m, reaction tube is cooled by molten salt forced to circulate by pump, reaction gas feed gas concentration is 40.8g / m 3 , Airspeed 1500h -1 , when the molten salt temperature is 360°C, when the inlet gas temperature is 353°C and the bed depth is 0.8 meters, the hot spot temperature of the catalytic bed is 383.8°C, and when the bed depth is 2 meters, it is...

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Abstract

The invention relates to fixed bed combined reaction equipment which mainly comprises a cylindrical shell with an end enclosure, a reaction gas inlet and a reaction gas outlet on the shell, a porous gas distributor, a porous gas collection plate, a catalyst layer and a heat exchange pipe for cooling media to transfer heat; steam headers provided with stream pressure adjusting valves form a cooling medium circular loop of which catalysts in at least one heat exchange reaction area are filled in the pipe. The fixed bed combined reaction equipment ensures that heat transfer is designed according to the requirement on the amount of the reaction heat transfer in the reaction, is used for the synthesis of methanol and dimethyl ether, methanation, F-T reaction, the preparation of phthalic anhydride by ortho-xylene oxidation and other strong-effect reaction processes, reduces the temperature difference, improves the reaction efficiency and the yield, saves energy, reduces consumption and achieves the large-sized aim.

Description

technical field [0001] The invention is a catalytic reaction equipment, which is used for fluid catalytic reaction and heat transfer process, belongs to the field of chemical engineering, and is especially suitable for synthesizing methanol, synthesizing dimethyl ether, Fischer-Tropsch reaction to produce liquid hydrocarbons and methane, o-xylene oxidation to produce ortho Strong reaction processes such as phthalic anhydride. Background technique [0002] For some strong exothermic reactions such as methanol synthesis, synthesis gas to dimethyl ether, Fischer-Tropsch reaction to liquid hydrocarbons and methane, o-xylene oxidation to phthalic anhydride, etc., in order to improve the reaction efficiency, it is necessary to remove the reaction heat at the same time. , For example, the Lurgi shell-and-tube methanol tower uses shell-side water to remove the heat of reaction in the reaction tube. In the shell-and-tube reactor design, the temperature of the coolant does not change ...

Claims

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Application Information

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IPC IPC(8): B01J8/02
Inventor 楼韧楼寿林
Owner 杭州林达化工技术工程有限公司
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