Method for starting methanol synthesis tower through reverse steam guiding
A technology of methanol synthesis tower and start-up method, which is applied in the field of methanol synthesis, can solve the problems of long start-up time of methanol synthesis tower, and achieve the effect of increasing service life and increasing output
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
specific Embodiment approach 1
[0015] Specific implementation mode one: (refer to attached Figure 1~3 ) The start-up method of the methanol synthesis tower of the present embodiment is carried out according to the following steps:
[0016] 1. Drain the water in the steam drum 3, reduce the liquid level of the methanol synthesis tower 2 shell side to 60% to 70% of normal production, and transfer the low-pressure steam in the steam pipe network to the methanol synthesis tower 2 Shell side, heating the synthesis catalyst in the tube side; at the same time, the medium-pressure steam from the conversion section is also input into the shell side of the methanol synthesis tower 2 through the steam ejector; the temperature of the catalyst is increased to be consistent with the temperature of the steam; the synthesis catalyst is copper-based catalyst;
[0017] Two, the compressed synthesis gas obtained after being compressed by the compressor passes through the shell side of the gas-gas heat exchanger 5, and passe...
specific Embodiment approach 2
[0021] Embodiment 2: The difference between this embodiment and Embodiment 1 is that in step 1, the liquid level in the shell side of the methanol synthesis tower is 60% to 70% of the height of the shell side of the methanol synthesis tower during normal production. Others are the same as the first embodiment.
specific Embodiment approach 3
[0022] Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that the water level in the steam drum during normal production in step 3 is 60% to 80% of the height of the steam drum. Others are the same as the first embodiment.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 