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

MVR evaporation capacity

2021-04-22View Original

Thread Content

When concentrating traditional Chinese medicine extracts using an MVR evaporation unit, the evaporation rate never reaches the designed level (the equipment is 90% new, and the impact of scaling on heat transfer is not taken into account). Could some experienced professionals in this field give some advice on what are the common factors that affect the evaporation rate of MVR?
Reply #22021-04-22
1. What is the compressor operation frequency? 2. Is the heat exchange area of the heat exchanger insufficient? 3. The evaporation area of the evaporator is insufficient!
Reply #32021-04-23
With a set of MVR units of the same specifications, the evaporation rate can meet the design requirements; therefore factors such as compressor frequency, heat exchanger area, and evaporator area can be disregarded. However, the operating current of the compressor is slightly low, and the outlet temperature is a bit high
Reply #42021-04-23
Different compositions of the solution result in different evaporation rates, as the boiling point changes. Generally, dilute solutions have lower boiling points and thus higher evaporation rates; once evaporation proceeds to a certain extent, an increase in the concentration leads to an elevation of the boiling point, after which the evaporation rate decreases.
Reply #52021-04-25
Is it related to the piping? The pipe resistance is different
Reply #62021-04-26
An increase in boiling point does affect heat transfer efficiency, but the amount of vaporization during initial evaporation remains unchanged, so it shouldn’t be due to the rise in boiling point.
Reply #72021-04-26
Firstly, the selection of pipes is based on steam pipeline standards and specific processes, which generally poses no issues. Secondly, another identical set of devices can also achieve the designed evaporation rate, so it should not be a piping issue. I think the problem lies with the compressor, but I don’t know much about compressors, so I’d like to hear the advice from those who are more experienced
Reply #82021-04-28
What type of compressor is it, centrifugal or positive-displacement?
Reply #92021-04-29
Haha, the problem has been solved. It’s not a compressor issue; it’s a fault with the flow meter. It was a misunderstanding. Thank you all for your guidance

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.