HCBBS Forum (English)
Submit Chemical Projects / Find Solutions
Amplify Your Requirements on a Broader Chemical Platform *Engineering · Technology · Equipment · Solutions*
Submit Request

【Question】Calculation of steam consumption

2024-06-04View Original

Thread Content

This post was last edited by ynothmql on 2024-6-4 at 16:25. I would like to ask how to calculate the steam consumption. For example, in a vertical container with a volume of 5 cubic meters, steam is introduced to raise the temperature inside the container from room temperature to 140°C, with a pressure of around 3.5 kg. Then one will want to know how much steam is needed and how long the heating will take. I just want to ask how to calculate it, or if there are any calculation plugins or tables or something like that. Only by knowing how to calculate it can I determine what size and how many steam vents to use. Another thing is, what generally determines the number of safety valves required? This is my first time working on tanks of this size; for smaller equipment in the past, one valve was sufficient. I would also appreciate it if the experts here could answer my questions. Thank you so much! I’d like to praise once again the way pages switch when clicked on this website – it’s extremely smooth; I really love it. Give the website designer a thumbs up! ! !
Reply #22024-06-04
If the tank contains air, when steam enters, the air is expelled. The size of the steam inlet is determined by the process requirements, that is, it is set according to the size of the pipes in the customer’s process system. The customer tells you the steam consumption, and you use this to calculate the safety valve.
Reply #32024-06-04
To determine the heating time accurately, it is recommended to take the following factors into consideration: 1. The heat dissipation of the container, which in turn depends on various factors such as ambient temperature, wind speed, humidity, the height at which the container is installed, its insulation properties, and the thickness of its walls. 2. The flow rate of steam entering the container; the process of steam entry is both a process of air displacement and a heat exchange process, and a lower steam flow rate results in a greater tendency for the temperature of the expelled air to rise.
Reply #42024-06-05
Well, on my end, the pipes at the client’s side used to be larger than the device’s air inlets; so reducers were used at the front end to reduce the diameter before the air entered the device.
Reply #52024-06-05
1. The steam consumption is calculated using the heat balance equation: Heat balance equation: Heat absorbed = Heat released. Heat released = Heat released during the superheating phase of the steam + Heat released during the latent heat phase of the steam + Heat released during the condensation phase of the steam. Expanding this, Q = C × M × Δt; these values are then substituted into the equation above. Where: C---specific heat, J/(kg·℃); M---mass flow rate, kg/s; Δt---temperature difference, ℃. If steam is mixed directly into the medium, then the formula above applies. In the case of heat exchange through a steam gap, it is necessary to calculate the heat exchange area. The area is calculated using the formula: Q = K × A × ΔT, where K is the overall heat transfer coefficient, in W/(㎡·℃); A is the heat exchange area, in ㎡; and ΔT is the effective average temperature difference, in ℃. For rough estimates, the value of K can be determined using empirical values based on the operating conditions. ΔT can be replaced by the logarithmic mean temperature difference multiplied by a correction factor of 0.9. After calculating the area, compare it with the area inside your tank; if they are similar, it’s acceptable. If there’s a large difference, adjust the flow rate and recalculate. Finally, determine the time based on the flow rate, and determine the pipe diameter based on the flow rate. 2. The number of safety valves is related to the amount of safety discharge required. If one safety valve can provide sufficient discharge, then one is enough. If one safety valve cannot deliver enough discharge, or if the valve is too large, multiple safety valves can be used in parallel.
Reply #62024-06-06
Okay, thank you. I’m looking into it
Reply #72024-06-15
To calculate the steam consumption, you need to know the heat loss of the container, the specific heat capacity of steam, and its thermodynamic properties. First, it can be estimated by following these steps: 1. Calculate the heat required between the initial and target temperatures of the air inside the container. The formula Q = m*c*ΔT can be used, where m is the mass, c is the specific heat capacity, and ΔT is the temperature change. 2. Considering potential heat losses in actual operation, the heat calculation value should be increased appropriately. 3. Calculate the required amount of steam based on the enthalpy difference of the steam (vaporization latent heat). You can consult a steam table to obtain these data. 4. The calculation of heating time requires taking into account the steam heat transfer rate and the heat exchange characteristics of the container. As for software tools, some engineering calculation software such as MATLAB or specialized thermodynamics calculation software can be used to facilitate more accurate calculations. Regarding the installation of safety valves, the number required is usually determined by the size of the container, its design pressure, and the maximum pressure it may experience. It is recommended to refer to relevant pressure vessel design standards or consult experienced engineers. For specific calculations and designs, it is recommended to consult professional engineers or technical support to ensure safety and accuracy. .

Submit a Project

**Looking for Chemical Technology, Equipment & Solutions?** No Registration Required Broader Platform Exposure | Global Chemical Service Provider Connections

Submit Request — Free Consultation

Disclaimer

This is an automated machine translation of the original thread. Some technical terms may have inaccuracies; the original text shall prevail. Click "View Original" at the top right to access the source page, which supports IP-based automatic real-time language translation. Please watch out for contact details and sales inducements to prevent fraud. All content and translations are for reference only, representing solely the poster's personal views. For enquiries, email service@hcbbs.com.