Water Environment Federation (WEF) Discussion Forums
Home      Members   Calendar   Who's On
Welcome Guest ( Login | Register )
      

Home » WEF Discussion Forums » Biosolids & Residuals » sludge drying

19 posts, Page 2 of 2. ««12

sludge dryingExpand / Collapse
Author
Message
Posted 4/25/2007 1:14:00 PM
Supreme Being

Supreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme Being

Group: Forum Members
Last Login: 6/26/2008 9:18:16 PM
Posts: 372, Visits: 708
Sure -- When you sample the dried sludge and put in a drying oven for a sufficient time. the dried weight should be at least 90% of the original sample weight (i.e., 10% or less moisture.)

David
Post #4901
Posted 10/17/2007 10:32:37 AM
Forum Newbie

Forum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum Newbie

Group: Forum Members
Last Login: 10/17/2007 10:25:03 AM
Posts: 2, Visits: 1
What David is refering to is the final product (Dried biosloids). 90% solids or better is the goal for most "Class A" drying facilities. Meaning that there is 10% or less residual moisture remaining in the final product.

Matt
Post #7070
Posted 10/17/2007 10:47:02 AM
Forum Newbie

Forum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum Newbie

Group: Forum Members
Last Login: 10/17/2007 10:25:03 AM
Posts: 2, Visits: 1
I have found that non digested solids pose some operational problems. Primary sludge in general could cause various issues with sticking, clogging, etc. (not fun). If you receive biosolids from more than one source operators will be faced with constant changes in operational parameters. It is a definite challenge when your plant is receiving sludge from different plants. 

Matt
Post #7071
Posted 10/26/2007 12:32:12 PM


Forum Member

Forum MemberForum MemberForum MemberForum MemberForum MemberForum MemberForum MemberForum Member

Group: Forum Members
Last Login: 6/3/2008 12:53:23 PM
Posts: 39, Visits: 105
wsclifton (4/20/2007)
Jeff,

I am interested in all types of sludges, but have had sticking problems with a straight waste activated that is dewatered (prior to drying) to about 22% solids using about 25 pounds per dry ton of polymer conditioning.

One comment I heard was that an anaerobically digested sludge drys the best, with waste activated second and raw primary/waste blend third. Not sure about this and was hoping for some feedback.

steve


I wouldn't worry to much about how the differences between anaerobic vs. waste activated sludge unless you are designing a new facility. Most of us are stuck with what we got. Both anaerobic and aerobic digested sludge are suitable for sludge dryers. Neither works great if the digestion is incomplete.

Indicator organisms may not be destroyed if incomplete digestion occurs. There are some interesting papers floating around that discuss regrowth and reactivation, etc. I don't think anybody tests for pathogens. We only test for indicator organisms.

Is the sticky sludge causing an issue? How ofter is the unit cleaned? Is it run continuously or batch?



Post #7244
Posted 1/12/2008 8:11:59 AM
Forum Newbie

Forum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum Newbie

Group: Forum Members
Last Login: 1/12/2008 8:38:02 AM
Posts: 1, Visits: 2
---

I've noticed a new technology. At least it is new for me:
Check this page about Sludge Drying Technologies:
http://sdt-h.eu/web/index.php?lang=english

The so called ELODE (Electro-Osmosis Dehydrator) seems to be good. Did you hear about it before? What's your opinion about it?

Thanks

Peter
Post #7975
Posted 1/14/2008 1:36:15 PM
Supreme Being

Supreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme BeingSupreme Being

Group: Forum Members
Last Login: 6/26/2008 9:18:16 PM
Posts: 372, Visits: 708
Not a long list of references -- apparently only one sewage works.  I cannot tell whether this technology produces an EQ quality of product or not.  And I don't think I'll be buying a product from Hungary anytime soon.

David
Post #7986
Posted 1/17/2008 11:31:25 AM
Junior Member

Junior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior Member

Group: Forum Members
Last Login: 4/11/2008 11:44:04 AM
Posts: 10, Visits: 40
We have a dryer that we use for WAS that is thickenend and then dried.  Our biggest problem is not with the dryer but the dewatering.  Can't get much above 9% with the unit we have.  I have operated this unit for about 18 months and it works well considering.  We are changing our dewatering unit to improve performance with the dryer and save money.  The dried product looks like dirt and doesn't have much of an odor unless it gets burnt.  Coliform results have been ND.
Post #8024
Posted 2/8/2008 4:59:36 AM
Junior Member

Junior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior MemberJunior Member

Group: Forum Members
Last Login: 2/29/2008 3:07:09 AM
Posts: 18, Visits: 16
There is a company called Flo-dry in New Zealand that makes dryers. They use a complex system of blending dried, partdried and feed sludge and separate fines from the pellets and reblend.

But are such dryers Greenhouse Gas monsters? I guess if you are a big plant > 10 mgd, or cold climate then the economies of scale justify.

For smaller plants what about solar driers. Has the technology survived its brief entry onto the scene? We looked at solar driers for a temperate climate and were looking at a drying area based on 4 kgH2O/m2.day. The driers cost about $880 000 per 1000m2.

Solar drying manages to disinfect both E.coli and Salmonella. The sludge typically gets up to 40 or 50 degC.

We were drying liquid sludge from a lagoon - up to a soil like consistency. In this configuration you dont need any polymer. You can load them with belt press sludge if you want faster drying - the economies probably favour this.

Regards

Grant H, Australia

Post #8297
Posted 2/26/2008 9:15:08 AM
Forum Newbie

Forum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum NewbieForum Newbie

Group: Forum Members
Last Login: 4/9/2008 11:59:43 AM
Posts: 7, Visits: 24
I thought the thermal drying pathogen reduction required a certain time above a certain temperature.  We've got an Andritz going in and I think in order to meet 503 we have to maintain 200F at the discharge end of the drum. 
Post #8498
« Prev Topic | Next Topic »

19 posts, Page 2 of 2. ««12

Reading This TopicExpand / Collapse
Active Users: 1 (1 guest, 0 members, 0 anonymous members)
No members currently viewing this topic.

PermissionsExpand / Collapse

All times are GMT -5:00, Time now is 12:06pm

Powered By InstantForum.NET v4.0.0 © 2008
Execution: 0.234. 10 queries. Compression Enabled.