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May 20th, 2013, 2:29pm
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Trickling Fliter Loadings (Read 489 times)
A Beak
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Trickling Fliter Loadings
Jan 03rd, 2012, 12:08pm
 
Hello.  I am wondering if anyone knows of any textbook minimum loading numbers for a "roughing" trickling filter.  I think I am looking for gpd/ft3 but lbs/ft3 could be useful as well.  Out plant has a two stage biological process that consists of the roughing filter followed by 2 diffused air ABs.  I feel confident that even without the filter we would get adaquate treatment from just the AB's and i have slowly been diverting flow away from the RF to conserve energy.  I am worried that the growth in the filter will dry out and cause odor/operational issues.  Any advice would be appreciated.
Thanks

Alex
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biogataw
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Re: Trickling Fliter Loadings
Reply #1 - Jan 3rd, 2012, 1:05pm
 
Hello Alex,

we have a biotrickling filter treated H2S air!
We used an inert plastic packing.
To give you an idea for the level of a low water sprinkling rate, in our developmental period we drive our test plant with 1,2 m³/m²(BTF-column)/d!
BR
biogataw
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A Beak
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Re: Trickling Fliter Loadings
Reply #2 - Jan 3rd, 2012, 1:53pm
 
Thanks!  To be more specific, our typical daily flow is around 2.5-3.0 MGD and our trickling fliter is 60 ft in diameter with 18 feet of media.
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biogataw
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Re: Trickling Fliter Loadings
Reply #3 - Jan 3rd, 2012, 2:21pm
 
Hello Alex,


I understand that you BTF diameter is 60 ft (18,3 m) and the packing height is 18 ft (5,5m) and the flow rate is 2,5 to 3,0 MGD (ca. 9,5 m³/h)!

Do you need the  biotrickling filter for cleaning waste water or waste gas?
BR
biogataw
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Jeff Naumann
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Re: Trickling Fliter Loadings
Reply #4 - Jan 3rd, 2012, 2:22pm
 
Check out page 3 of the following EPA Fact Sheet:

http://nepis.epa.gov/Exe/ZyNET.exe/P10099PA.TXT?ZyActionD=ZyDocument&Client=EPA&Index=2000+Thru+2005&Docs=&Query=&Time=&EndTime=&SearchMethod=1&TocRestrict=n&Toc=&TocEntry=&QField=&QFieldYear=&QFieldMonth=&QFieldDay=&IntQFieldOp=0&ExtQFieldOp=0&XmlQuery=&File=D%3A%5Czyfiles%5CIndex%20Data%5C00thru05%5CTxt%5C00000025%5CP10099PA.txt&User=ANONYMOUS&Password=anonymous&SortMethod=h%7C-&MaximumDocuments=1&FuzzyDegree=0&ImageQuality=r75g8/r75g8/x150y150g16/i425&Display=p%7Cf&DefSeekPage=x&SearchBack=ZyActionL&Back=ZyActionS&BackDesc=Results%20page&MaximumPages=1&ZyEntry=1&SeekPage=x&ZyPURL
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A Beak
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Re: Trickling Fliter Loadings
Reply #5 - Jan 4th, 2012, 9:03am
 
It is for wastewater.
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Re: Trickling Fliter Loadings
Reply #6 - Jan 4th, 2012, 10:01am
 
Hallo Alex,

I ´ve 18 years operation experience with waste gas!

BR
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Re: Trickling Fliter Loadings
Reply #7 - Jan 4th, 2012, 2:29pm
 
A roughing filter would be designed for 100-300 lb BOD/d/1000 cu ft/day. High rate media (used in roughing filters) should have a minimum wetting rate of 0.7 gpm/sq foot.

reference WEF manual of practice 11 Volume II: liquid processes

hope this helps,

Ryan
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Re: Trickling Fliter Loadings
Reply #8 - Jan 4th, 2012, 3:05pm
 
Hello together,

it looks so, that the limits for BTF´s in waste water and waste gas systems the same!

waste water:  0,70      gpm/ft²      =      1,7      m³ / (m²*h)
waste gas:     0,49      gpm/ft²      =      1,2      m³ / (m²*h)
BR
biogataw
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A Beak
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Re: Trickling Fliter Loadings
Reply #9 - Jan 5th, 2012, 7:14am
 
Thanks for the good info.  What about temporarily taking the tower offline?  How long can it stand with no flow before we would start having issues?  I don't know if this makes a difference but it is currently around -6 degrees C outside.
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Eric Raj
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Re: Trickling Fliter Loadings
Reply #10 - Jan 5th, 2012, 8:48am
 
At those low temps odor will not be a problem initially.  You really need to check daily on whether or not odors are beginning to arise.  AB's use more energy than TF's, so I would look to run the TF as efficiently as possible in order to limit how much air must be applied to the AB's.

~Eric
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A Beak
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Re: Trickling Fliter Loadings
Reply #11 - Jan 5th, 2012, 10:08am
 
Energy consumption is the main reason i want to take it offline for a few days to see if it does save energy.  Right now we are using between 2 and 4 75 hp pumps to feed the tower and we have a 50 hp and a 75 hp high efficency turbo blower.  I realize that taking the tower offline would cause the blowers to run faster and would consume more energy.  Right now the the 50 hp blower runs at its minimum speed almost all the time and we still have a final DO of about 3 ppm.  What i am currious about is if the super efficient blower at a higher speed will consume more than running the old biofilter pumps pumping all the flow to the top of our tower.  Is there anyway to estimate any of this without actually having to make such a drastic change?  
Also on an unreated topic:  Does this forum have a built in spell check by any chance?  I am pretty much mentaly impared when it comes to spelling.
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Eric Raj
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Re: Trickling Fliter Loadings
Reply #12 - Jan 5th, 2012, 11:39am
 
To a rough extent you can estimate through some calculations what your electric usage is.  But you ought to measure the load on the blower in realtime under the conditions which you wish to know about.  Age of blower and other components in the system all will affect electrical usage.  

Sadly, I have not found any spell check option on this site.

~Eric
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A Beak
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Re: Trickling Fliter Loadings
Reply #13 - Jan 10th, 2012, 1:30pm
 
Thanks again for the responses.  Right now we are operating with no recyle at all gonig through the tower.  That is saving us from pumping roughly 3 mgd.  Measuring soluable BOD going in and out of the tower i am getting 55 ppm going in and 8 going out.  Settleability is still good and our effluent quality has not changed at all.  This is saving us between 10 and 20 KW/day even with the blower running at a faster speed.  The thing that i am worried about now is the distribution over the media.  The distribution system is powered by the flow out of the arms.  When the pump speed gets too low the arms stop moving.  This only seems to happen for a few hours in the early morning when flow is at its lowest.  Can this poor distribution cause us any problems with the growth on the tower?  Thanks

Alex
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Re: Trickling Fliter Loadings
Reply #14 - Feb 15th, 2012, 6:45am
 
With appropriate loadings the low-rate trickling filter, such as main and additional sedimentation models, should remove from 80% to 85% of the used BOD.  While there is some unloading or sloughing of solids at all times, the significant unloadings usually happen several times a year for relatively short intervals.  
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