How to control the 1.0Mpa pipeline network throughout the plant
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In companies with an excess of steam at 1.0 Mpa, how should the pressure in the 1.0 Mpa pipeline network be controlled? Should it be relieved through the thermal power plant or through a certain unit? Are there any other good methods?
The choice of vent location: the noise generated by venting can be quite loud; will this affect the workers’ ability to work?； When performing venting, it is also necessary to consider whether there is any stagnation of steam in the pipeline network, as well as whether there is an excess amount of steam in the network – whether this excess is due to the waste heat generated by the facility or for some other reason. In such cases, the steam should be sent back to the power plant for venting ； It is still the case that steam is supplied from outside the power plant, which leads to the need for venting; these actions can affect the operation of the system. Therefore, the choice of the appropriate location for venting must be made after taking into account the overall operating conditions of the system.
In the long term, using turbines to replace high-power motors can effectively solve the aforementioned problems~~
How to do it? Could you explain it in more detail?
Here, some steam is released from the thermal power plant, and then further vented from the catalysis workshop, as the other workshops do not have steam venting pipelines installed
It’s all money being placed there; in our company, doing something like this would definitely result in a fine. In winter, to prevent freezing, no vapor is allowed to be present. It’s better to do the calculations
Yeah, so I’m going to ask around to find out what the situation is for everyone, and after that I’ll prepare a plan
I agree with the view from the 5th floor: using a steam engine instead of an electric motor, or employing a steam turbine for power generation, is more energy-efficient. It’s a shame to let that energy go to waste; one ton of steam is worth over 200 units, and if one ton is produced per hour, that amounts to two million units per year.
For the steam of this grade that is released, does the power plant have an external supply system for steam of this grade? I mainly want to understand the specific reasons for venting steam at this level.