Innovative Technologies for Treatment of Malodors in Sustainable - - PowerPoint PPT Presentation

innovative technologies for
SMART_READER_LITE
LIVE PREVIEW

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


slide-1
SLIDE 1

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 7123, Fax: 2358 0054, E-mail: kekyeung@ust.hk

slide-2
SLIDE 2

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.

slide-3
SLIDE 3

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.

slide-4
SLIDE 4

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

slide-5
SLIDE 5

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

slide-6
SLIDE 6

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

slide-7
SLIDE 7

Field Study – HKUSTCampus

Performance study of biocidal gel technology under practical useconditions

Inhibit microbial growth

slide-8
SLIDE 8

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

slide-9
SLIDE 9

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.

slide-10
SLIDE 10

Field Study – DSDSite

Performance study of biocidal gel technology under realsituation Rainwater drainage line at JordanValley

slide-11
SLIDE 11

Field Study – DSDSite

Performance study of biocidal gel technology under realsituation

upstream midstream downstream

slide-12
SLIDE 12

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.

slide-13
SLIDE 13

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

slide-14
SLIDE 14

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

slide-15
SLIDE 15

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

slide-16
SLIDE 16

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%

slide-17
SLIDE 17

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

slide-18
SLIDE 18

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

slide-19
SLIDE 19

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

slide-20
SLIDE 20

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.

slide-21
SLIDE 21

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
slide-22
SLIDE 22

Thank You Thank You Thank You Thank You