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What considerations should be taken into account for the equipment layout of towers and thermosyphon reboilers?
When arranging the equipment for the tower and the reboiler at the bottom of the tower, the following should be taken into account: 1. The reboiler should be placed as close to the tower as possible, with the pipe ends of the reboiler even being directly connected to those of the tower. If the reboiler is connected directly to the tower, and there is an instrumentation interface between the two pipe connections on the P&ID diagram, then that instrumentation interface should be arranged so that the equipment is installed at either of the connected pipe connections. 2. Usually, the reboiler is installed on a separate bracket or frame; if it needs to be fixed to the tower body, consultation with the equipment specialists is required. The location and type of supports rooted on the tower shall be capable of meeting the requirements imposed by the displacements and stresses resulting from the expansion of the tower and pipelines. At this time, it is also necessary to consider providing the tower with the required reboiler operation and maintenance platforms. 3. The support position of the reboiler should be determined such that the upward displacement of the connection port between the reboiler and the tower is the same. Once the support location is determined, it should be promptly communicated to the equipment team. 4. A column with dual reboilers, whose reboilers should be arranged symmetrically.
The height at which the reboiler is located should be proportional to the liquid level in the tower bottom to ensure stable process operation!
As long as the installation height of the reboiler is not too high, it is independent of the liquid level in the tower bottom.
The main consideration is to keep the heights of the two as consistent as possible; of course, the distance between them should neither be too great nor too small, as either extreme makes piping difficult.
The height at which the reboiler is located should be proportional to the liquid level in the tower bottom to facilitate stable process operation
The vapor pipe connecting the bottom of the tower to the reboiler should be stress-free, in order to prevent vibrations caused by liquid entrapment during siphoning. Appropriate clearance should be provided between the height of the reboiler’s tube sheet and the lower end of the vapor connection pipe in the tower
The distance between the center of the vapor line connecting the bottom of the tower to the reboiler and the reboiler tube sheet should not be too large, to avoid poor thermosiphon effect and subsequent impact on the reboiler’s efficiency. The reboiler should be placed as close as possible to the tower to minimize piping length and reduce piping resistance.
For vertical siphon reboilers, the normal liquid level in the reactor bottom is usually at about the same level as the upper tube sheet of the reboiler. To accommodate fluctuations in the liquid level, it is necessary to leave an appropriate margin between the height of the reboiler’s tube sheet and the lower end of the pipe connecting to the vapor phase of the tower. What do you typically use as a suitable value for this margin? What is the reason for choosing such a large size? (Is it determined by the degree of change in the amount of gasification?) )
What does \"proportional to\" mean? Could you explain it in detail?
Unless there are special requirements, the side of the tube side and the material inlet of the tower are often connected directly, as the reboiler outlet contains a vapor-liquid mixture (with a vaporization rate of around 10% to 15%), which results in less resistance when facilitating material circulation. At the top of the reboiler, an elbow should be added in the middle to connect them, which provides better stress distribution. Another factor to consider is that the height of the upper tube sheet in a vertical thermosyphon reboiler is generally required to be lower than the liquid level in the tower; at most, it can be at the same level. The tube box of the reboiler cannot be designed to be very long. If the range of control over the tower’s liquid level is large, and the side of the reboiler’s tube side is connected directly to the tower inlet, there is a risk of liquid backflow; in such cases, it is necessary to connect the top of the reboiler to the tower inlet.