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Reboiler steam condensate pressure

2026-06-20View Original

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This post was last edited by xbl240 on 2026-6-21 at 21:22. It is a combined unit; the medium-pressure steam pressure in the system is 1.1 MPa. There is 1 medium-pressure steam condensate recovery tank (0.4 MPa). The secondary steam generated through flashing is fed into the low-pressure steam network. During startup, some of the condensate from the reboilers can be discharged into the condensate recovery tank, while some other condensate, due to its low pressure, cannot be discharged there. After the steam is condensed in the reboiler, its pressure drops. How can one determine by how much the pressure of this condensate has decreased? Can the condensate generated by the reboiler be drained in? I would like to ask the experts here.
Reply #22026-06-23
The question posed by the original poster is quite typical. To clarify: once medium-pressure steam enters the reboiler, the pressure loss on the steam side depends mainly on the pressure drop across the heat exchange tubes in the reboiler itself, the resistance in the outlet pipes and valves, as well as the pressure in the condensate recovery tank. In simple terms, the condensate outlet pressure is approximately the inverse of the sum of the recovery tank pressure, the static head, and the pipeline friction losses; however, the key to being able to discharge the liquid into the recovery tank lies in whether the backpressure at the reboiler outlet is lower than the self-priming pressure difference of the condensate. Here are a few suggestions for reference: Check whether there is a steam trap or control valve at the outlet of the reboiler; if a steam trap is installed, it will maintain a certain backpressure (usually 0.05~0.2 MPa higher than the pressure in the recovery tank), and the condensate is discharged due to this pressure difference ; If not, the condensate pressure is the reboiler shell-side pressure minus the frictional losses in the pipes; it may be close to or even lower than the pressure in the recovery tank, making it impossible to discharge the condensate. Check whether there is air blockage or excessive length in the condensate pipeline: Some of the condensate fails to flow out, and common reasons for this are U-shaped bends in the pipeline, insufficient head difference, or overly thin pipes, which prevent the condensate from overcoming the pressure in the recovery tank. It is recommended to calculate the static pressure difference from the outlet of each reboiler to the recovery tank (for example, the condensate from reboilers located at a higher level can rely on gravity, while additional considerations are needed for those located at a lower level). It is recommended to conduct a simple pressure distribution test: temporarily install pressure gauges at several typical reboiler condensate outlets to measure the condensate pressure under different operating conditions, and by comparing it with the pressure of 0.4 MPa in the recovery tank, it can be determined whether the issue lies in an excessive pressure drop within the reboiler itself or in pipeline resistance. If it is the latter, considering installing a condensate pump or adjusting the pipeline slope may be advisable. Additionally, in the initial stage of operation, the system is not yet stable; there are significant fluctuations in steam flow and temperature, and it is normal for the condensate pressure to fluctuate as well. It is recommended to conduct tests only after the system has stabilized. If multiple reboilers are operated simultaneously, it is also necessary to ensure that the collector pipes are large enough to prevent interference between them. The above is an analysis based on general engineering principles; it is best to calculate the specific values by referring to your pipeline diagrams and equipment specifications.

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