Innovative Technologies for Treatment of Malodors in Sustainable - - PowerPoint PPT Presentation
Innovative Technologies for Treatment of Malodors in Sustainable - - PowerPoint PPT Presentation
Innovative Technologies for Treatment of Malodors in Sustainable Drainage System Prof King Lun Yeung Department of Chemical and Biomolecular Engineering & Division of Environment Hong Kong University of Science and Technology Tel.: 2358
Situation:
1. Malodor is a prevalent problem in densely populated urban centers due to ageing infrastructure; 2. It is a complex problem due to large range of compounds involved, their low concentration and transient nature as well as individual sensitivity.
Problem:
1. H2S and other malodor compounds are nuisance and pose a health risk; 2. They are source of citizen complaints and are difficult to treat; 3. H2S in sewer can cause sewer corrosion as well as fatalities.
Approach:
1. Control SRB (sulfur reducing bacteria) activities in sewer; 2. Room temperature catalytic treatment of malodorous compounds (i.e., H2S and NH3).
H2S + 1/2 O2 → H2O + 1/8 S8 NH3 + 3/4 O2 → 3/2 H2O + 1/2 N2
Description of Technology:
TEOS Acid solution Hydrolysis Mixing Combine Age Gel Mixing
1. The controlled-release gel that continuously dose biocides and inhibitors that specifically target microorganisms causing malodor; 2. Only safe and U.S. FDA/EPA approved materials are used; 3. The controlled-release gel is designed to last for at least 30 days and work under aggressive environment found in sewer and drainage system.
Cu2+ Fe3+ NO -
3
Colloidal silica ClO2 Acids Combine Biocidal hydrogel
4 8 28 12 16
Time(day)
20 24 5 15 25 35
Cumulative ClO2 Released (%)
b
double-SiO2S14 double-SiO2S15
Field Study – HKUSTCampus
Performance study of biocidal gel technology under practical useconditions
BiocidalHydrogels Pictures of the biocidal hydrogels with (a) PVA-SiO2 and (b) double-SiO2 frameworks.
Bactericidal properties of hydrogels
BactericidalReduction Day 1 Day7
Aerobic Anaerobic Aerobic Anaerobic
SiO2 99.9 99.9 99.0 98.0 PVA-SiO2 95.0 97.0 90.0 90.0 double-SiO2 95.0 94.0 92.0 95.0 Note: Bactericidal tests were carried out at room temperature using 105 CFU/ml of E. coli and 105 CFU/ml of Desulfobulbus propionicus.
3
90-160 m /h
Field Study – HKUSTCampus
Performance study of biocidal gel technology under practical useconditions
Inhibit microbial growth
600 400 200 800 Jan Feb Mar Apr May Jun
H2S concentration (ppb)
control control test
Field Study – HKUSTCampus
Performance study of biocidal gel technology under practical useconditions
Suppresses H2S generation
Summary
9 weeks HKUST Site
2-weeks Background Period: Average H2S level = 180 ppb with the maximum level = 480 ppb. 5-weeks Test Period:
A 200 gram sample treats an estimated 90,000 m3 sewer water in 30 days (Average flow of 125 m3/h)
Suppress H2S below olfactory threshold (< 40 ppb) Decreases malodor generating anaerobic bacteria by 60 %. 2-weeks Post-Test Period: Average H2S level = 150 ppb with the maximum level = 250 ppb.
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation Rainwater drainage line at JordanValley
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation
upstream midstream downstream
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation
Starting date: 8th Dec End date: 19th Feb
Background
The H2S concentration in the sewer were recorded on site and bacteria growthanalysis were performed in HKUST by taking samples on-site for4-weeks.
Testing
A porous container with multi-functional gel were put into the sewer. Study was done for 5-weeks so as to investigate the duration of effectiveness on malodorremoval.
Post-testing
A 2-week study will be performed to evaluate the post-effect after removal of thegel.
H2S level was monitored by 2 HONEYWELL H2S Gas Detectors per location. 3 water samples were taken each week and measured at HKUST.
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation Midstream (location2)
midstream
Average : 3.3 ppm Maximum : 5.5 ppm 0 ppm 0 ppm 2.2 ppm 7.0 ppm
2 4 6 8 10 12 14 8 16 24 32 40 48 56 64 72 H2S concentration (ppm) Days Average Highest Background Test Post-Test
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation Midstream (location2)
midstream
Day Aerobic (*10^4cfu/ml) Anaerobic (*10^4cfu/ml) 26 40 2 3.8 18 5 9.0 7 1.2 2.3 9 2.8 4.1 13 10 6.0 15 6.8 3.0 19 15 5.8 21 87 74 28 19 15 28* 3.5 3.8 27 16 9.3 35 0.4 1.2 40 0.3 0.2 43 0.2 0.2 49 0.7 0.9 56 3.0 0.7 66 6.5 9.3 73 14.8 3.5
10 20 30 40 50 60 8 16 24 32 40 48 56 64 72 Bacteria Count (104 cfu/ml) Day Aerobic Anaerobic Background Test Post-Test
Field Study – DSDSite
Performance study of biocidal gel technology under realsituation
Average : 3.0 ppm Maximum : 5.5 ppm 0 ppm 0 ppm 1.7 ppm 3.0 ppm
1 2 3 4 5 6 7 8 9 10 8 16 24 32 40 48 56 64 72 H2S concentration (ppm) Day Average Highest Background Test Post-Test 1 2 3 4 5 6 7 8 9 10 8 16 24 32 40 48 56 64 72 H2S concentration (ppm) Days Highest Average Background Test Post-Test
3.4 ppm 6.0 ppm 0 ppm 0 ppm 2.2 ppm 5.0 ppm
Summary
11 weeks DSD Site
4 weeks Background Period: Average H2S level = 3.0 ppm, 3.3 ppm and 3.4 ppm in up, mid, down streams. The maximum level =7ppm. 5 weeks Test Period: H2S level dropped to below 1 ppb in all streams 2-weeks Post-Test Period: Average H2S level = 0.6ppm, 2.0ppm and 1.8 ppm in up, mid, down streams. The maximum level =3.0ppm, 7.0ppm and 4.0ppm in up, mid, down streams.
Aerobic bacterial concentration (104 CFU/ml) Anaerobic bacterial concentration (104 CFU/ml) Upstream Midstream Downstream Upstream Midstream Downstream Background 3.5 31 16 4.2 27 11 Testing 3.4 1.3 1.7 4.0 1.0 1.2 Reduction 3% 96% 89% 5% 96% 89%
Description of Technology:
1. Novel room temperature catalysts that convert H2S and NH3 into harmless minerals, water and N2; 2. Operates under high humidity (100 % R.H.) and dark conditions; 3. Long and stable operating life under extreme
- perating conditions found in drainage system.
3
catalyst SiO2 sol Gel Humidity-resistant catalyst
H2S Malodor Treatment
Performance study of the Novel Catalyst was carried out under:
A saturated vapor (23.76 mmHg) at 25oC (x ppm H2S, 3.05% H2O, 19.8% O2 , 76.9% N2)
300 600 900 0.1 1.0 5.0 10.0 15.0
Vanadium loading (wt. %) H2S Conversion Rate
(µ µ µ µmol1s-1g-1)
b
aerogel
Note: the reaction was carried out for a 400 sccm 33.3 ppm H2S in air at room temperature (298 K) over 25 mg catalyst. The Novel Catalysts contain 15 wt.% of vanadia catalyst (i.e., 3.75 mg catalyst). 0.2 0.4 0.6 0.8 1 10 20 30 40
Conversion [H2S] ppm
VT10, 25mg, wet 25 mg 100 mg
Novel Catalyst
NH3 Malodor Treatment
Performance study of the Novel Catalyst was carried out under:
A saturated vapor (23.76 mmHg) at 25oC (0.22% NH3, 3.05% H2O, 19.8% O2 , 76.9% N2)
10 20 30 40 50 60 1.0 5.0 15.0
NH3 Conversion Rate
(µ µ µ µmol1s-1g-1)
Vanadium loading (wt. %)
a
aerogel
Note: the reaction was carried out for a 400 sccm 2183 ppm NH3 in air at room temperature (298 K) over 25 mg catalyst. The Novel Catalysts contain 15 wt.% of vanadia catalyst (i.e., 3.75 mg catalyst).
Olfactory threshold
Novel Catalyst
Concluding Remarks
1. The controlled-release gel is a fast-acting and effective technology for malodor suppression for water drainage system; 2. The gel can be easily deployed in problem area and has a long lastingeffect; 3. The cost of the gel is low and 200 gram (= 0.2 L) gel is able to suppress H2S in sewer flow of 120 m3/h treating 90,000 m3 of drainagewater; 4. 10-30 % of aerobic bacteria remained viable during the 30 daytests. 5. A Novel Catalyst was shown to be effective in suppressing airborne H2S and NH3 malodor at room temperature and high humidity situation.
Acknowledgement
We would like to acknowledge the financial supports from the Hong Kong Innovation and Technology Fund (ITS/188/01), the Hong Kong Environment and Conservation Fund/Woo Wheelock Green Fund. We are also grateful for the help and advice from the Hong Kong Drainage Services Department. This talk includes works by:
- Mr. Kei Bo CHEUNG
- Mr. Long Ting LUK
- Dr. Hao CHEN
- Prof. Wei HAN