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Investment-saving ammonia synthesis process and device

A technology of ammonia synthesis and ammonia synthesis tower, which is applied in the field of ammonia synthesis, can solve the problems of rising equipment investment and high equipment cost, and achieve the effect of lower design temperature and lower investment

Active Publication Date: 2013-09-25
CHINA CHENGDA ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] At the same time, with this process, the temperature (2) of the inlet gas entering and leaving the tower heat exchanger determines the design temperature of the heat exchanger entering and leaving the tower. The higher the design temperature, the higher the equipment cost. When the design temperature is greater than 200°C, The heat exchangers entering and exiting the tower need to use high-grade materials, and the equipment investment will increase in steps

Method used

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  • Investment-saving ammonia synthesis process and device
  • Investment-saving ammonia synthesis process and device
  • Investment-saving ammonia synthesis process and device

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Such as image 3As shown, an ammonia synthesis process that saves investment includes an internal heat exchange ammonia synthesis tower, and its inlet and outlet heat exchange devices (inlet and outlet tower heat exchangers). The synthesis tower enters the tower gas and synthesizes the tower gas to exchange heat. The synthetic gas entering the tower passes through the tube side of the import and export heat exchange device, and the synthesized tower gas passes through the shell side of the import and export heat exchange device. The tube sheet and the tube box are separated, the tube side is connected through the tube box, and the shell side is connected through the connecting pipe. The outlet of the low temperature section is set on the tube box connecting the tube side of the low temperature section and the high temperature section, and a part of the synthetic gas entering the tower is exchanged from the inlet and outlet. The outlet of the low-temperature section of ...

Embodiment 2

[0038] An investment-saving ammonia synthesis device, comprising an internal heat exchange type ammonia synthesis tower, and its inlet and outlet heat exchangers, the inlet and outlet heat exchangers are respectively provided with synthesis tower gas inlet and outlet and synthesis tower gas inlet and outlet, The synthetic gas entering the tower passes through the shell side of the import and export heat exchanger, and the synthesized tower gas passes through the tube side of the import and export heat exchanger. The inlet of the synthesized tower gas is connected with the outlet of the synthesized tower gas of the internal heat exchange ammonia synthesis tower, There are two outlets for the synthetic gas entering the tower at the shell side of the import and export heat exchanger, which are the outlet of the high temperature section and the outlet of the low temperature section. The outlet of the high temperature section of the internal heat exchange ammonia synthesis tower is ...

Embodiment 3

[0043] This embodiment is basically the same as Embodiments 1 and 2. The inlet and outlet heat exchangers are divided into a low-temperature section and a high-temperature section. The low-temperature section and the high-temperature section are separated by a tube sheet and a tube box. The tank is connected, and the shell side is connected through a connecting pipe. The difference is that the synthesized gas enters the tower through the shell side of the inlet and outlet heat exchangers, the synthesized tower gas passes through the tube side of the inlet and outlet heat exchangers, and the outlet of the low temperature section is set on the connecting pipe connecting the shell side of the low temperature section and the high temperature section.

[0044] Such as Figure 6 Shown: The tube side of the inlet and outlet heat exchangers is designed as two sections A and B, and the two sections are separated by different tube sheets. Section A and section B can adopt different des...

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Abstract

The invention discloses an investment-saving ammonia synthesis process and device. The device comprises an internal heat exchange type ammonia synthesis tower, and an inlet / outlet heat exchanger, wherein synthetic tower inlet gas and synthetic tower outlet gas which enter and exit the internal heat exchange type ammonia synthesis tower are subjected to heat exchange through the inlet / outlet heat exchanger; the inlet / outlet heat exchanger is divided into a high-temperature section and a low-temperature section; part of the synthetic tower inlet gas is extracted out from an outlet of the low-temperature section of the inlet / outlet heat exchanger and is fed into a shell pass annular space of the internal heat exchange type ammonia synthesis tower; the residual synthetic tower inlet gas is extracted out from the high-temperature section of the inlet / outlet heat exchanger and is fed into the internal heat exchange type ammonia synthesis tower; a shell and the interior of the internal heat exchange type ammonia synthesis tower have different design temperatures; the design temperature of the shell is lower than that of the interior part of the tower. The invention discloses the ammonia synthesis process and device which can save more investment compared with the prior art.

Description

technical field [0001] The invention belongs to the field of ammonia synthesis and is suitable for an ammonia synthesis process and device using an internal heat exchange type ammonia synthesis tower. Background technique [0002] The current ammonia synthesis technology mostly adopts the internal heat exchange type ammonia synthesis tower, which also uses the import and export heat exchange device to exchange heat between the synthetic input gas and the synthetic output gas entering and exiting the internal heat exchange ammonia synthesis tower. The feed gas containing H2 and N2 generates ammonia through synthesis reaction. The reaction process is carried out in a reactor (ammonia synthesis tower) filled with a catalyst under high pressure conditions. On the one hand, the ammonia synthesis catalyst needs to reach a certain temperature condition (activation temperature) to have catalytic activity, and high temperature can speed up the reaction; on the other hand, the ammoni...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01C1/04
Inventor 许斌刘勇跃王时川
Owner CHINA CHENGDA ENG
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