Print page

Home » How does filtered water differ from reverse osmosis water?

Print page

How does filtered water differ from reverse osmosis water?

Q: I work in a bio-ethanol production plant equipped with a multi-pressure distillation system.

In order to decrease the cost of water treatment, we are going to change the process water (which is mainly used in the fermentation section) from a good quality water (reverse osmosis) to the filtered water having the following data:

EC:2920 µs
TDA:1500 µs/cm
TURBIDITY:0.6
Cl2:0.5 ppm

I would appreciate if you could advise me whether the aforementioned water is good for the distillation system and why?

What are disadvantages with the distillation equipment (e.g., heat exchangers) using this water?

A: This is really out of my area of expertise, so take my reply with a ton of dissolved salt. I don’t know how much this filtered water differs from the reverse osmosis water you are now using. I am assuming it has more and different impurities than the RO water.

If this water is re-circulated through the process it may cause deposits in the condensers and re-boilers as the impurities buildup. And the metallurgy should be able to tolerate the Cl2. I think you suspect there could be problems in these areas. I think you should contact a water treatment company and get their advice and help in monitoring the water quality in the distillation unit. As these trace concentrations buildup it may also affect the VLE.

Here are more of the latest questions on: Distillation

Is there a guideline for setting the height of the conical section of a column?
I have designed a column with two sections of different diameters (enriching section 1,900 mm and stripping section 3,500 mm). Is there any rule or guideline to be followed to set the height of conical section of column between these two diameters? Presently I have considered height of conical section as 500 mm approx (equivalent to one manhole) between these two diameters.

Is vacuum distillation best to recover iso amyl alcohol and manufacturing esters?
I'm planning to set up a distillation unit for distilling fusel oil to recover iso amyl alcohol and manufacturing esters from it. I've been suggested to go for vacuum distillation through use of watering pump and reboiler of falling film evaporator type. The column will be about 10m high having a diameter of 0.6m. Is this the right way to go? Which packing should I consider? Will vacuum distillation break the azeotrope formed between water and ethanol?

Is there a good way to calculate the height of stage in a distillation column?
I'm working on a distillation column for a six-part multi-component distillation column. It contains structured packing. I estimated about eight stages with a model and came up with approximately the same answer with pseudo-McCabe-Thiele. I was careful to pick the correct heavy key and light key. Then, I realized I did not have a good way to calculate the height of stage. The model, like most, only tells you the number of stages not the height of stage or Z, the final height of theoretical packing.

Kister would say 1-3 feet as an assumption (based on gas resistance), or I could estimate it using a KG or KL. Empirical data would help.

I assume that the oil, a collection of C10+, would pose the greatest resistance, which makes calculating an H stage even more difficult. The feed is trace water, toluene and oils.

Any advice or reference that might be useful in solving this dilemma?

How do I calculate the void space in a column?
How do I calculate the void space in a column? Actually we are putting ½-inch balls in a 14-inch pipe. Height of packing will be 3 inches. Above the ½-inch balls we will put ¼-inch balls and the packing height will be the same (3 inches). How many balls can I put in the column?

How does a water draw off vessel work?
I need to design water draw off vessel. How does a water draw off vessel work?

Back to Ask the Experts

More content on this topic:

Featured Sponsor