Development of Organic Waste Treatment Facilities, Phase
2
Environmental Impact Assessment Report
Chapter Title
Tables
Table 3.1:__ Hong Kong Air
Quality Objectives
Table 3.2:__ Proposed
New Hong Kong Air Quality Objectives (as announced 17 January 2012)
Table 3.3:__ Proposed
Air Quality Standards
for Other Potential Emissions
Table 3.4:__ Representative
ASRs Identified for Assessment
Table 3.6:__ Key Dust Emission Factors to be adopted in the Assessment
Table 3.7:__ Process
comparison between OWTF 1 and OWTF 2
Table 3.8:__ Operational
Emissions comparison between OWTF 1 CHP and OWTF 2 CHP
Table 3.9:__ Operational
Emissions comparison between OWTF 1 and OWTF 2 odour treatment units
Table 3.10:_ Operational
Emissions comparison between OWTF 1 flare and OWTF 2 flare
Table 3.11:_ Traffic Flows of Man Kam To Road and Kong
Nga Po Road
Table 3.12:_ Vehicle
Classification in the EMFAC-HK Model
Table 3.14:_ Construction
modelling results summary (Tier 1 mitigated scenario)
Table 3.15:_ Cumulative
operation modelling results summary (Mitigated)
Table 3.16:_ Cumulative
operation modelling results summary (Mitigated)
Figures
Figure 3.1 Locations
of Air Sensitive Receivers
Figure 3.2 Locations
of Potential Construction Dust Sources
Figure 3.3a Locations
of ISCST3 Sources
Figure 3.3b Locations
of Caline4 Sources
Figure
3.5a 2012 Observed Traffic Flows
Figure
3.5b Distribution of OWTF Phase
2 Development Traffic
Figure 3.6 Cumulative
Result - Contour of Daily RSP Concentration (µg/m³) at 1.5m above ground during
operational phase for CHP and Odour Treatment
Appendices
Appendix 3.1: Emission calculation for construction dust
Appendix 3.2: Data Input for FDM model
Appendix 3.3: Calculation of Dust Suppression Efficiency
Appendix 3.4: Vehicle Classification
Appendix 3.5: Vehicle Population
Appendix 3.6: Projected Growth
Appendix 3.7: Traffic Flow for 2017
Appendix 3.8: Trips and VKT for Hong Kong
Appendix 3.9: Trips and VKT for OWTF2
Appendix 3.10: Temperature and Relative Humidity
Appendix 3.11: Emission Factors
Appendix 3.12: TSP Construction Phase Results
Appendix 3.13: Operational Phase results (ASR)
This section presents the assessment of potential air quality impacts associated with the construction and operational phases of the proposed Organic Waste Treatment Facility – Phase 2 (OWTF 2). Dust generated from construction activities is the primary concern during the construction phase. During the operation phase the major sources of air pollution include, but are not limited to: emissions from burning generated biogas in a combined heat and power (CHP) plant; emissions from an odour treatment unit, which is used to treat odorous emissions, and; emissions from flaring, under equipment outages.
Representative Air Sensitive Receivers (ASRs) within 500 m of the subject site have been identified and the worst case impacts on these receivers will be assessed. Suitable mitigation measures, where necessary, have been recommended to protect the nearby sensitive receivers and to achieve the legislative criteria and guidelines.
The criteria and guidelines for evaluating air quality impacts are laid out in Annexes 4 and 12 of the Technical Memorandum on Environmental Impact Assessment Ordinance (EIAO-TM), respectively.
The principal legislation for the management of air quality is the Air Pollution Control Ordinance (APCO) (Cap 311). The APCO specifies Air Quality Objectives (AQOs) which stipulate the statutory limits of air pollutants and the maximum allowable numbers of exceedence over specific periods. The AQOs are shown in Table 3.1.
Table 3.1: Hong Kong Air Quality Objectives
Pollutant |
Averaging Time |
AQO
concentration (µg/m³) |
Allowable
exceedences |
Sulfur Dioxide (SO2) |
1
hour |
800 |
3 |
24
hour |
350 |
1 |
|
Annual |
80 |
0 |
|
Total Suspended Particulates (TSP) |
1
hour(1) |
500 |
3 |
24 hour |
260 |
1 |
|
Annual |
80 |
0 |
|
Respirable Suspended Particulates (PM10) |
24 hour |
180 |
1 |
Annual |
55 |
0 |
|
Nitrogen
Dioxide (NO2) |
1
hour |
300 |
3 |
24 hour |
150 |
1 |
|
Annual |
80 |
0 |
|
Carbon
Monoxide (CO) |
1
hour |
30,000 |
3 |
8 hour |
10,000 |
1 |
|
Ozone
(O3) |
1
hour |
240 |
3 |
Lead |
3
month |
1.5 |
0 |
Note (1) EIAO-TM,
not an AQO
Table 3.2: Proposed New Hong Kong Air Quality Objectives (as announced 17 January 2012)
Pollutant |
Averaging Time |
AQO concentration (µg/m³) |
Allowable exceedances |
Sulfur Dioxide (SO2) |
10 minute |
500 |
3 |
24 hour |
125 |
3 |
|
Respirable Suspended Particulates (PM10) |
24 hour |
100 |
9 |
Annual |
50 |
0 |
|
Fine Suspended Particles (PM2.5) |
24 hour |
75 |
9 |
Annual |
35 |
0 |
|
Nitrogen Dioxide (NO2) |
1 hour |
200 |
18 |
Annual |
40 |
0 |
|
Carbon Monoxide (CO) |
1 hour |
30,000 |
0 |
8 hour |
10,000 |
0 |
|
Ozone (O3) |
8 hour |
160 |
9 |
Lead |
Annual |
0.5 |
0 |
Total Suspended Particulates (TSP) |
1 hour(1) |
500 |
- |
There is the potential for emissions that are not covered by the EPD’s AQOs. These emissions may arise if the biogas generated is consumed onsite in the CHP or during emergency use of the flare. The air quality standards for various other potential pollutants are proposed by making reference to overseas standards, as detailed in Table 3.3.
Table 3.3: Proposed Air Quality Standards for Other Potential Emissions
Pollutant |
Averaging Time |
Air
Quality Standards (µg/m³) |
Reference |
Hydrogen Chloride |
1 hour |
2,100 |
Cal/EPA Acute reference level from Office
of Environmental Health Hazards Assessment, California |
Annual |
20 |
Integrated Risk Information System, USEPA |
|
Hydrogen Fluoride |
1 hour |
240 |
Cal/EPA Acute REL |
Annual |
14 |
California, OEHHA (2005) |
|
Volatile Organic Compounds (Methane) |
1 hour |
600,000 |
TEEL-0 (the threshold concentration below
which most people will experience no adverse health effects) from Office of
Health, Safety and Security, US Department of Energy |
The existing and planned representative Air Sensitive Receivers (ASRs) that could be affected by the Project within 500 m from its site boundary have been identified and are summarised in Table 3.4. The locations of ASRs and the boundary of 500 m study area are shown in Figure 3.1. It should be noted that one of the ASRs required to be assessed in the Study Brief, namely the Police Border District Headquarters, is outside the 500 m boundary from the Project site.
Table 3.4: Representative ASRs Identified for
Assessment
Description |
Existing/ Proposed |
Type of Use |
Height above ground (m) |
Horizontal distance from
study area boundary (m) |
Construction Phase |
Operation Phase |
|
A1 |
Temple |
Existing |
Temple |
1.5 |
163 |
P |
P |
5 |
|||||||
10 |
|||||||
A2 |
Village House No. 308, Sha Ling |
Existing |
Residential |
1.5 |
36 |
P |
P |
5 |
|||||||
10 |
|||||||
A3 |
San Uk Ling Holding Centre |
Existing |
Office |
1.5 |
204 |
P |
P |
5 |
|||||||
10 |
|||||||
A4 |
Village House No. 257, Sha Ling |
Existing |
Residential |
1.5 |
214 |
P |
P |
5 |
|||||||
10 |
|||||||
A5 |
Village House, Sha Ling |
Existing |
Residential |
1.5 |
26 |
P |
P |
5 |
|||||||
10 |
|||||||
A6 |
Village House, Sha Ling |
Existing |
Residential |
1.5 |
17 |
P |
P |
5 |
|||||||
10 |
|||||||
A7 |
Village House, Sha Ling |
Existing |
Residential |
1.5 |
166 |
P |
P |
5 |
|||||||
10 |
|||||||
A8 |
Police Dog Unit and Force Search Unit Training School |
Existing |
Office |
1.5 |
374 |
P |
P |
5 |
|||||||
10 |
|||||||
A9 |
Hong Kong Police Force Border District Headquarters |
Existing |
Office |
1.5 |
600 |
P |
P |
5 |
|||||||
10 |
|||||||
A10 |
Rifle range |
Existing |
Office |
1.5 |
289 |
P |
P |
5 |
|||||||
10 |
|||||||
A11 |
House 1,Proposed Kong Nga Po Residential Development |
Proposed |
Residential |
1.5 |
368 |
O |
P |
5 |
|||||||
10 |
|||||||
15 |
|||||||
A12 |
House 2,Proposed Kong Nga Po Residential Development |
Proposed |
Residential |
1.5 |
330 |
O |
P |
5 |
|||||||
10 |
|||||||
15 |
|||||||
A13 |
House 3,Proposed Kong Nga Po Residential Development |
Proposed |
Residential |
1.5 |
334 |
O |
P |
5 |
|||||||
10 |
|||||||
15 |
|||||||
A14 |
Assumed Village House 1, Proposed Hung Lung Hang Residential |
Proposed |
Residential |
1.5 |
484 |
O |
P |
5 |
|||||||
10 |
|||||||
15 |
|||||||
A15 |
Assumed warehouse 1, Proposed Man Kam To Development Corridor |
Proposed |
Office |
7 |
269 |
O |
P |
9.8 |
|||||||
12.6 |
|||||||
A16 |
Assumed warehouse 2, Proposed Man Kam To Development Corridor |
Proposed |
Office |
7 |
189 |
O |
P |
9.8 |
|||||||
12.6 |
|||||||
A17 |
Assumed warehouse 3, Proposed Man Kam To Development Corridor |
Proposed |
Office |
7 |
193 |
O |
P |
9.8 |
|||||||
12.6 |
|||||||
A18 |
Village House No. 62, Sha Ling |
Existing |
Residential |
1.5 |
440 |
P |
P |
5 |
|||||||
10 |
|||||||
A19 |
Village House, Sha Ling |
Existing |
Residential |
1.5 |
385 |
P |
P |
5 |
|||||||
10 |
The latest 5-year-average (2007 – 2011) ambient concentrations of pollutants measured at the closest EPD monitoring station to the proposed Project site, i.e., EPD’s Tai Po monitoring station, are noted for reference in Table 3.5.
Table 3.5: 5-year Annual Average Concentration at Tai Po Air Quality Monitoring Station (Year 2007-2011)
Pollutant |
5-year Average Concentration
(μg/m3) |
Current Annual AQO |
Sulfur Dioxide (SO2) |
12 |
80 |
Nitrogen
Dioxide (NO2) |
48 |
80 |
Total
Suspended Particulates (TSP) |
68 |
80 |
Respirable Suspended Particulates (PM10) |
48 |
55 |
It can be seen that the 5-year average air pollutant levels are in compliance with the current annual AQOs. Nevertheless, with the Government’s on-going and planned programmes to tackle various air pollution issues in Hong Kong, it is anticipated that the future background air quality would be improving. To predict the future background air pollutant concentration, the Pollutants in the Atmosphere and the Transport over Hong Kong (PATH) model, has been used.
The PATH model was updated in December 2012. This version is considered to be appropriate to use, as there have been no updates since the model release.
OWTF 2 is expected to receive and
process up to 300 tonnes of source-separated
organic waste for treatment each day. It is proposed
that the OWTF 2 will produce biogas as a source of
renewable energy and a compost / soil conditioner for use in landscaping,
agriculture or horticulture. The biogas can
be used as an energy source in its own right or be
used to generate heat and electricity for OWTF
2 with surplus exported to the power grid.
The
construction of the Project will involve
demolition and removal of the existing above ground structures of the Sha Ling Livestock Waste Composting Plant
(SLCP), and the construction of an building and supporting infrastructure and
civil engineering works. The main building will house technical,
administration, and control areas, an environmental education centre, and
pre-treatment and processing facilities, including reception bunker, conveyors,
pulpers, grit separation and storage tanks. Process
structures will include hygienisation units,
digesters, composting system, wastewater and air treatment plants; and
facilities for biogas storage, processing, utilisation and transmission etc. It
is anticipated that the proposed construction work of OWTF 2 site will be fully
completed and commissioned in 2017.
During construction, the major activities that would generate construction dust emissions include the following:
¡ Site clearance;
¡ Demolition and removal of the existing above ground structures;
¡ Excavation activities;
¡ Foundation works;
¡ Movement of mobile plant and vehicles on haul roads;
¡ Storage of potentially dusty construction materials;
¡ Installation of process equipment and storage tanks; and,
¡ Construction of superstructure.
The number of working days per month and number of working hours per day of the Project are anticipated to be 26 days and 12 hours, respectively, and no construction work is anticipated to be carried out on Sundays. Therefore, these assumptions would be adopted in the model calculation.
Prediction of dust emissions has been based on emissions factors from the Compilation of Air Pollution Emission Factors (AP-42), 5th Edition published by the US Environmental Protection Agency (USEPA). Based on, Section 13.2.3.3 of AP-42, the emission factor for a typical heavy construction activity is 2.69 megagrams (Mg)/hectare/month of activities. Based on Table 11.9-4 of AP-42, the emission factor of wind erosion is 0.85 megagrams (Mg)/hectare/year. Areas of heavy construction are to have mitigation measures applied, namely watering, to reduce dust emissions.
Dust emissions during construction can be
suppressed by regular water spraying on site. In general, water spraying twice
a day could reduce dust emission from active construction area by 50%. However,
for the Project, more frequent water spraying is proposed. Watering eight times
per day, or once every 1.5 hours, is suggested at all active works areas in
order to achieve a higher dust suppression efficiency of 87.5%. Active
construction activities include construction of roads, drilling, ground
excavation, cut and fill operations (i.e. earth
moving), etc.
Emission factors for stockpiles are calculated according to Section 13.2.4.3 of AP-42, and the associated factor of wind erosion is based on Table 11.9-4 of AP-42. It should be noted that, the stockpiles are anticipated to be 80% covered with impervious sheeting to reduce windblown dust. The key dust emission factors are summarised in Table 3.6.
Full calculations of the construction dust emissions can be found in Appendix 3.1.
Table
3.6: Key
Dust Emission Factors to
be adopted in the Assessment
Activities |
Value |
Unit |
Reference |
Heavy
construction activities including all above ground and open construction
works, excavation and slope cutting works |
2.69 2.39494E-04 2.99368E-05 |
Mg/hectare/month g/m²/s (unmitigated) g/m²/s (mitigated) |
Section
13.2.3.3 AP-42,
5th Edition |
Wind
erosion from heavy construction |
0.85 2.69533E-06 |
Mg/hectare/year g/m²/s |
Table
11.9-4 AP-42,
5th Edition |
Stockpiles – disturbed |
5.97336E-07 1.19467E-07 |
g/m²/s (unmitigated) g/m²/s (mitigated) |
Section 13.2.4.3 AP-42, 5th Edition E=k*0.0016*[(U/2.2)1.3/(M/2)1.4] |
Stockpiles – wind erosion |
0.85 2.69533E-06 5.39066E-07 |
Mg/hectare/year g/m²/s (unmitigated) g/m²/s (mitigated) |
Table
11.9-4 AP-42,
5th Edition |
Construction of the OWTF 2 is expected to
commence in the first quarter of 2015. Based
on current available information, the proposed/committed projects that may have
cumulative effects during the construction phase of the Project include:
¡ Cement Mixer Plant (no construction details);
¡ Proposed Man Kam To Development Corridor (no construction details);
¡ Columbarium, Crematorium and related facilities at Sandy Ridge Cemetery as recommended under the “Land Use Planning for the Closed Area Feasibility Study” (construction period 2019 – 2022)
¡ Proposed comprehensive development on Kong Nga Po Road (no construction details);
¡ Proposed residential development in Hung Lung Hang (no construction details); and
¡ If biogas export to the gas grid is considered, construction of a 200mm diameter biogas pipeline.
Where construction programmes are known, cumulative assessment has been conducted. However, projects identified are generally in early development (recommended or feasibility) and there is currently no information regarding the construction program or emissions that the construction of these projects may produce. Sandy Ridge development has a construction timetable, however the coincurrent effects are not anticipated due to the differing construction period to OWTF 2. The projects listed are therefore not assessed in this EIA and would need to be included in studies conducted by the project proponent.
OWTF 2 will include construction of a rising main to transfer sewage flows to the existing Sha Ling pumping station, minor modification of the access road to accommodate swept path of RCVs accessing the site, and may include construction of a gas pipeline connection running from the site along the Kong Nga Po road to the existing NENT Landfill / Tai Po Synthetic Natural Gas (SNG) pipeline. Air quality impacts will be confined to the construction phase when trenching works and minor road modifications may be carried out. As the works are of short duration and subject to standard construction dust mitigation measures, any potential construction dust is expected to be mitigated to an acceptable level of impact.
During the operation phase, there would be
air quality impacts on the ASRs due to:
¡ Emissions from odour treatment unit;
¡ Exhausts from CHP;
¡ Emissions from flaring; and,
¡ Existing and proposed open roads outside the OWTF 2 area but within the 500 m study area.
To estimate the emissions from the odour treatment unit, CHP and flaring of OWTF 2, reference has been made to the emissions data from the OWTF Phase I (OWTF 1) because both OWTF 1 and OWTF 2 share similar process designs as compared in Table 3.7 and discussed below.
The comparison shows that a similar process capacity, of 200-300 t/d would be used. The same digestion method is proposed and feedstocks are both likely to mainly consist of food waste. The total capacity of the OWTF 1 and OWTF 2 digestion tanks are similar at around 13,000m3 and 16,000m3 respectively. Although the retention time in the digesters varies, the biogas produced is expected to be similar due to the same digestion process and similar feedstocks.
The energy generation for both OWTF 1 and OWTF 2 are proposed to be Combined Heat and Power (CHP). Both are to have a gas treatment system, prior to use in the CHP, to reduce hydrogen sulfide content. Due to the similar gas produced in the digestion stage, the emissions from the CHP are expected to also be similar.
Both Phases propose an aerobic tunnel system for composting the dewatered digestate from the digestion tanks. Processing time in the composting plant of the different Phases is two to three weeks. Due to the nature of the feedstocks, the resulting compost and associated emissions from this process are expected to be similar.
As the biogas produced is expected to be of a similar nature, the emissions from flares are also expected to produce comparable concentrations of assessed contaminants.
From the comparison of OWTF 1 and OWTF 2 it can be seen that the processes and associated products and emissions would be expected to be of similar nature. Therefore it is reasonable to make reference to the emission information from OWTF 1 where it is not available for OWTF 2. Where emission data is available for both OWTF 1 and OWTF 2, the maximum of either value is adopted in order to be conservative. Details of the emission information used for this assessment are discussed in the following sections.
Table 3.7: Process comparison between OWTF 1 and OWTF 2
Process |
OWTF 1 |
Reference1 |
OWTF 2 |
Reference2 |
Waste received |
200 t/d |
s1.4 |
300 t/d |
s3.4.2 |
Digestion |
||||
· Digestion type |
Wet anaerobic digestion |
s2.27 |
Wet anaerobic digestion |
s3.1 |
· Digester size |
Five x 2,660 m3 |
s2.30 |
Total 16,000 m3 |
s3.4.2 |
· Retention time |
40 days |
s3.18 |
24 days (dependent on biogas yield, waste composition, final digestion method, footprint) |
s3.4.2 |
Energy Generation |
||||
· Generation type |
Combined Heat and Power (CHP) |
s2.31 |
Combined Heat and Power (CHP) OR Boiler |
s3.2.3 |
· Capacity |
N/A |
|
|
|
· Digester gas pre‑treatment to generation |
Gas cleaning unit for removal of hydrogen sulfide (H2S |
s3.19 |
Gas cleaning unit for removal of hydrogen sulfide (H2S) |
s3.2.3 |
Composting |
||||
· Process |
Aerobic Tunnel composting |
s3.22 s2.30 |
Aerobic Tunnel composting |
s3.5 s3.5 |
· Capacity (final compost) |
5,500 t/year |
|
15,300 t/year |
|
· Retention time (composting) |
about 2 weeks |
s3.22 |
7 days |
|
· Retention time (curing) |
14 days |
|||
Gas Treatment |
||||
· Energy generation exhaust treatment |
Desulfurisation (absorption) |
s2.31 |
Thermal process -
Carbon monoxide (CO), Total
hydrocarbons (THC), formaldehyde and methane (CH4) removal Catalyst Treatment - 80 – 90% H2S reduction - 50 – 100 mg/Nm3 Nitrogen oxides (NOx) |
s3.6.2 |
· Odour treatment unit |
Scrubber and biofilter |
s2.32 |
Biofilter and Active Carbon Filter - 0.25 ppm H2S - 0.25 ppm Ammonia - 0.25 ppm Mercaptans OR UV-C and Ozone Technology (recommended) - 90 – 98% odour unit reduction |
s3.6.2 |
Flare |
||||
· Usage |
Emergency use in the event of energy generation failure |
s2.31 |
Emergency use in the event of energy generation failure |
s3.4.2 |
(1) AECOM, December 2009. Organic Waste Treatment Facilities Phase 1 – Feasibility Study. Environmental Impact Report. Hong Kong
(2) Mott MacDonald, June 2012. Development of Organic Waste Treatment Facilities Phase 2 – Feasibility Study Preliminary Design of OWTF. Hong Kong
The
preliminary design incorporates a combination of thermal and catalytic treatment
processes to remove pollutants from the exhaust gasses from the gas cleaning
unit and CHP. Following thermal and catalytic treatment, the exhaust
will be vented via the flue stack. The
design emission rates for the CHP are shown in Table 3.8. Emissions that may need to be considered are listed as
follows:
¡ Dust
¡ Carbon Monoxide (CO)
¡ Nitrogen Oxides (NOx)
¡ Sulfur Dioxide (SO2)
¡ Volatile Organic Compounds (VOCs)
¡ Hydrogen Chloride (HCl)
¡ Hydrogen Fluoride (HF)
Table 3.8: Operational Emissions comparison between OWTF 1 CHP and OWTF 2 CHP
Equipment |
Parameter |
Units |
OWTF 1 |
OWTF 2 |
Value used for OWTF 2
assessment |
Notes |
|
Energy Generation |
|
||||||
|
Flowrate |
Nm3 |
2,500 |
2,500 |
2,500 |
Flowrate is a maximum |
|
|
Temperature |
°C |
460 |
not available |
460 |
|
|
|
RSP |
mg/Nm3 |
15 |
not available |
15 |
|
|
|
CO |
mg/Nm3 |
650 |
1,100 |
300(1) |
OWTF 2 - no gas cleaning |
|
200 300 |
|
OWTF 2 - with catalytic treatment OWTF 2 - with thermal |
|||||
|
NOx |
mg/Nm3 |
300 |
500 |
500(1) |
OWTF 2 - no gas cleaning |
|
500 100 |
|
OWTF 2 - with catalytic treatment OWTF 2 - with thermal |
|||||
|
SO2 |
mg/Nm3 |
50 |
15 |
15 |
|
|
|
VOC |
mg/Nm3 |
150 |
not available |
150 |
|
|
|
HCl |
mg/Nm3 |
10 |
not available |
10 |
|
|
|
HF |
mg/Nm3 |
1 |
not available |
1 |
|
|
(1) Worst-case of two post gas-treatment technologies
The proposed odour treatment
system for the OWTF 2 involves all stages taking place within enclosed
facilities or process treatment housings which are under negative pressure. The
air from the reception, preparation and pre-treatment areas, the mixing tank,
and the composting plant will be ventilated using a fan and duct system. The ventilated air will be treated to remove
odours and dust prior to venting through the flue stack.
The proposed odour treatment system is a two stage process involving either a biofilter, or ultraviolet light (UV-C) together with ozone treatment as the first stage, and an activated carbon filter as the second stage. It is recommended to install the UV-C and ozone treatment system with second stage active carbon filters as this has lower footprint and maintenance requirements than the option of using a biofilter. The design emission rates of the odour treatment unit are shown in Table 3.9.
Table 3.9: Operational Emissions comparison between OWTF 1 and OWTF 2 odour treatment units
Equipment |
Parameter |
Units |
OWTF 1 |
OWTF 2 |
Value used for OWTF 2
assessment |
Notes |
||
Odour treatment unit |
|
|||||||
|
Flowrate |
Nm3/h |
not available |
195,000 |
195,000 |
Flowrate is a maximum |
||
|
Temperature |
°C |
35 |
50 |
35 |
Maximum temperature from odour treatment unit. Lower value used as this give worse thermal dispersion |
||
|
VOCs (include NMVOC) |
mg/Nm3 |
680 |
not available |
680 |
|
||
|
RSP |
mg/Nm3 |
6 |
not available |
6 |
|
||
|
Odour |
OU/Nm3 |
300 |
500 |
50 |
OWTF 2 includes NH3 and H2S and is based on no gas cleaning |
||
50 |
|
OWTF 2 includes NH3 and H2S and is based on UV-C and Ozone technology |
||||||
|
Dust |
mg/Nm3 |
not available |
<10 |
10 |
|
||
In the event of a system outage with the
CHP, the biogas would need to be flared to protect the system from
over-pressure. The gas flare system
will be capable of accommodating all of the gas produced at the facility, in
case of an emergency. The design emission rates for the flare are shown
in Table
3.10.
Emissions that may need to be considered are listed as follows:
¡ Dust
¡ Carbon Monoxide (CO)
¡ Nitrogen Oxides (NOx)
¡ Sulfur Dioxide (SO2)
¡ Volatile Organic Compounds (VOCs)
¡ Hydrogen Chloride (HCl)
¡ Hydrogen Fluoride (HF)
Table 3.10: Operational Emissions comparison between OWTF 1 flare and OWTF 2 flare
Equipment |
Parameter |
Units |
OWTF 1 |
OWTF 2 |
Used in OWTF 2 assessment |
Notes |
|
Flare |
|
||||||
|
Flowrate |
Nm3/h |
not available |
1,500 |
1,500 |
Flowrate is a maximum |
|
|
Temperature |
°C |
900 |
not available |
900 |
|
|
|
RSP |
mg/Nm3 |
5 |
not available |
5 |
|
|
|
CO |
mg/Nm3 |
100 |
not available |
100 |
|
|
|
NOx |
mg/Nm3 |
200 |
not available |
200 |
|
|
|
SO2 |
mg/Nm3 |
50 |
not available |
50 |
|
|
|
VOC |
mg/Nm3 |
21 |
not available |
21 |
|
|
|
HCl |
mg/Nm3 |
10 |
not available |
10 |
|
|
|
HF |
mg/Nm3 |
1 |
not available |
1 |
|
|
Additional traffic is expected to occur
south of the Kong Nga Po / Man Kam To
Road intersection. The portion of Man Kam To Road that lays within the study area is to the north of
this junction, and so, no additional traffic due to the OWTF 2 is expected at
this portion.
Table 3.11: Traffic Flows of Man Kam
To Road and Kong Nga Po Road
Major Road |
AM
Peak Traffic Flow (pcu/h) |
PM
Peak Traffic Flow (pcu/h) |
Man Kam To
Rd – 2012 observed traffic flow |
1521
(i.e.866+655 for 2-way traffic) |
1199
(i.e.679+520 for 2-way traffic) |
Kong Nga Po Rd – 2012 observed traffic
flow |
210 (i.e. 68+142 for 2-way traffic) |
209 (i.e. 65+144 for 2-way traffic) |
Kong Nga Po Rd - estimated increase in
traffic flow due to operation of OWTF 2 |
31 (i.e. 15+16 for 2-way traffic) |
30 (i.e., 15+15 for two-way traffic) |
The OWTF2 reference design assumes that there will be an average of 60 deliveries of source separated organic waste to the facility at Sha Ling each day in dedicated Collection Vehicles [2]. It is further assumed that OWTF 2 will be open to accept organic waste every day, 7 days a week between the hours of 7 am to 9 pm (14 hours) and that there would be a peak period for unloading in the morning and evening.
The projected maximum number of RCV arriving at OWTF during morning and evening peaks would be up to 6 vehicles per hour. Waste deliveries may comprise either conventional Refuse Collection Vehicles (RCV) or vehicles transporting purpose built containers that enclose the loose or bagged organic waste. The containment unit for organic waste during transportation (RCV or container) must be designed to prevent ingress of rainwater (reducing leachate generation) and leakage of leachate. The containment unit must be robust and made of a corrosion resistant material (stainless steel or high density / hard wearing plastic are preferred). These containment units will be sealable to ensure a water and air tight seal that prevents ingress of water or any escape of odour. Following discharge at the OWTF2 the waste transfer vehicles will pass through a cleaning process before leaving to remove potential for odour impact on the public highway.
It is anticipated that waste collection operators using OWTF2 will employ industry good practice in terms of operation and maintenance of vehicles engaged in the transport of organic waste [3]. Moreover, guidelines and good operating practices will be formulated to avoid odour nuisance arising from the operation of the facility and the transportation of organic waste. In view of this, odour emission from the waste collection vehicles during transportation of organic waste is therefore not anticipated.
As presented in Section 3.2, under the APCO, AQOs are stipulated for seven criteria air pollutants, namely, nitrogen dioxide (NO2),
sulfur dioxide (SO2), total suspended particulates (TSP), respirable suspended particulates (RSP), carbon monoxide
(CO), ozone and lead. Each of the seven criteria
pollutants has been reviewed for relevance as major air pollution sources of
the Project as follows.
Nitrogen Dioxide (NO2)
According to the “2011 Hong Kong Emission Inventory Report” published by EPD in March 2013, navigation and road transport are the top two major sources of nitrogen oxides (NOx) generated in Hong Kong, constituting respectively about 33% and 29% of the total NOx emission in 2011.
NOx is transformed to NO2 in the
presence of O3 under sunlight.
As summarised
in Table 3.5, the latest 5-year average of the annual NO2
concentration is about 60% of the corresponding AQO. Therefore, NO2 has been identified as a key air pollutant of
the emissions from both road traffic and OWTF 2 emissions, and has been
assessed against the relevant AQOs for this Project.
Respirable Suspended Particulates (RSP)
According to the latest statistics of “2011 Hong Kong Emission Inventory Report”, navigation and road
transport are the top two major sources of RSP in Hong Kong, accounting
for respectively about 37% and 19% of the total RSP emissions in 2011.
As summarised in Table 3.5, the latest 5-year average of the annual RSP
concentration in the urban area is about 87% of the corresponding AQO. Therefore, RSP has been identified as a key air pollutant of the
emissions from both road traffic and OWTF 2 emissions, and has been assessed
against the relevant AQOs for this Project.
Sulfur Dioxide (SO2)
According to the latest statistics of “2011 Hong Kong Emission Inventory Report”, 54% of total SO2 emission in Hong Kong is attributed to navigation while less than 1% of the total emission is
due to road transport. The
introduction of ultra low sulfur diesel for vehicle
fleet in 2000 has also helped to reduce the SO2
emission from road transport in Hong Kong. As summarised in Table 3.5, the latest 5-year average of the annual SO2
concentration in the urban area is about 15% of the corresponding AQO. While the 5-year average SO2
level appears to be well below the relevant AQO with a large margin, the OWTF 2
is expected to produce SO2 emissions. Therefore, SO2 has been identified as a key air pollutant of the emissions and has
been assessed against the relevant AQOs for this Project.
Ozone
According to the “Air
Quality in Hong Kong 2011” published by EPD [4], ozone is a major constituent of photochemical smog. It
is not a pollutant directly emitted from man-made sources but formed by
photochemical reactions of primary pollutants such as NOx and volatile organic compounds (VOCs) under sunlight. As it takes several hours
for these photochemical reactions to take place, ozone recorded in one place could be
attributed to VOC and NOx emissions from places
distant from the assessment site. Hence, ozone is a regional air pollution
problem. Therefore, unlike such air pollutants as NOx,,RSP and SO2, ozone is not a pollutant directly attributable to emissions from nearby process or road
traffic. As a result, ozone is not identified
as a key air pollutant for air quality impact assessment for this Project,
though it is one of the criteria pollutants under the AQO.
Carbon Monoxide (CO)
According to the latest statistics of “2011 Hong Kong Emission Inventory Report”, road transport and
navigation are the top two major sources of CO emissions in Hong Kong, contributing respectively to about 67% and 18% of the total CO emission in 2011. However, based on the “Air Quality in Hong Kong 2012
Preliminary Report” published by EPD [5], the highest 1-hour CO level and the highest 8-hour CO concentration in Yuen
Long are respectively 2,200 μg/m3 and 1,945 μg/m3, which are only 7% and 19% of the corresponding AQO respectively. While the CO levels appears
to be well below the relevant AQO with a large margin, the OWTF 2 is expected
to produce CO emissions. Therefore, CO has been identified as a
key air pollutant of the emissions and has been assessed against the relevant
AQOs for this Project.
Lead
Since leaded petrol was banned in Hong Kong on 1 April 1999, it is no longer considered as
a primary source in Hong Kong. According
to the “Air Quality in Hong Kong 2011” published by EPD, the ambient lead concentrations continued to linger at
very low levels during 2011 as in previous years, and the overall 3-month averages, ranging from 0.02 μg/m3 (in Kwun Tong and Tung Chung) to 0.104 μg/m3 (in Yuen Long), were well below the AQO limit
of 1.5 μg/m3. Therefore, it is not considered
as a key air pollutant for the operation phase air quality impact assessment.
Identified
Key Air Pollutants
Based on the above review results and information on pollutants emitted from the OWTF 2 (Section 3.5.3) and concurrent sources, the following key air pollutants are considered relevant to the project and have been assessed:
§ Dust
§ Carbon Monoxide (CO)
§ Nitrogen Dioxide (NO2)
§ Sulfur Dioxide (SO2)
§ Volatile Organic Compounds (VOCs)
§ Hydrogen Chloride (HCl)
§ Hydrogen Fluoride (HF)
§ Respirable Suspended Particulates (RSP/PM10)
§ Fine Suspended Particulates (FSP/PM2.5)
§ Odour
To assess construction phase impacts through air quality modelling, use of the air quality model Fugitive Dust Model (FDM) was required. In accordance with the EPD’s Guidelines on Choice of Models and Model Parameters, FDM was used to predict the air pollutant concentrations due to open dust source impacts, which are shown in Figure 3.2. Details of the emission rates from the activities are given in Appendix 3.1.
FDM
is a computerised air quality model specifically designed for computing the
concentration and deposition impacts from fugitive dust sources. The model is
generally based on the well-known Gaussian Plume formulation for computing
concentrations, but the model has been specifically adapted to incorporate an
improved gradient transfer deposition algorithm [6]. FDM is one of the air quality models
listed as commonly used for EIA studies by EPD in Guidelines on Choice of Models and Model Parameters.
Causality effects
Gaussian plume models assume pollutant material is transported in a straight line instantly (like a beam of light) to receptors that may be several hours or more in transport time away from the source. The model takes no account for the fact that the wind may only be blowing at 1 m/s and will have only travelled 3.6 km in the first hour. This means that Gaussian models cannot account for causality effects, where the plume may meander across the terrain as the wind speed or direction changes.
This effect is not considered to be significant for the OWTF 2 site as the site is small.
Low wind speeds
Gaussian-plume models ‘break down’ during low wind speed or calm conditions due to the inverse speed dependence of the steady state plume equation. These models usually set a minimum wind speed of 0.5 m/s or 1.0 m/s and ignore or overwrite data below this limit.
Straight-line trajectories
Gaussian models will typically overestimate terrain impingement effects during stable conditions because they do not account for turning or rising wind caused by the terrain itself.
This may result in conservative results for elevated ASRs.
Spatially uniform meteorological conditions
Gaussian models assume that the atmosphere is uniform across the entire modelling domain, and that transport and dispersion conditions exist unchanged long enough for the material to reach the receptor even if this is several kilometres away. In the atmosphere, truly uniform conditions rarely occur.
Although the site is small, variation in the meteorological conditions is expected due to the local terrain. However, as a full year is modelled, most conditions are expected to be modelled and therefore the results are considered reasonable.
No memory of previous hour’s emissions
In calculating each hour’s ground-level concentrations, Gaussian models have no memory of the contaminants released during the previous hours. This limitation is especially important for the proper simulation of morning inversion break-up, fumigation and diurnal recycling of pollutants.
Hourly meteorological data for a full year as extracted from the PATH model released by EPD in December 2012 (meteorological data year 2010, grid 25, 44) has been adopted for use in FDM and is considered to be the most up to date data available, and representative of the site wind data at OWTF 2.
Prediction of dust emissions is
based on emissions factors from the Compilation of Air Pollution Emission
Factors (AP-42), 5th Edition published by the US Environmental
Protection Agency (USEPA). The locations of assumed dust sources are
given in Figure 3.1.
The key dust emission factors adopted in FDM are summarised in Table 3.6.
With addition of the TSP background level of 67 µg/m³, which is the 5-year average TSP levels recorded in EPD’s Tai Po Air Quality Monitoring Station (see Table 3.5), the hourly, daily and annual TSP concentrations at the identified ASRs have been predicted and compared with the current hourly, daily and annual average TSP criteria of 500 µg/m3, 260 µg/m3 and 80 µg/m3 respectively.
Construction on the OWTF 2 site is expected
to be completed over approximately 21 months (with 6 months testing and
commissioning). However the FDM
assessment has been completed assuming a construction period of nine months as
a conservative approach. The emissions are applied for one full year to capture
seasonal conditions.
For
hourly and daily TSP, a tiered modelling approach may be adopted. Tier 1
assumes 100% active area for a given year is emitting TSP.
This Tier 1 scenario (i.e. assuming 100% active area for the OWTF 2) is
hypothetical and for screening purposes to
identify which ASRs may be subject to TSP concentrations above the relevant
standards. For the purpose of the Tier 1 screening, the
dust mitigation measures, including frequent water spraying, as detailed in Section 3.8.1.1,
are taken into account when estimating the dust emission rates from the
construction activities. Details of the
Tier 1 dust sources including their coordinates, dimensions and estimated
emission rates are detailed in Appendix
3.2.
Locations of the assumed dust sources for Tier 1 assessment are shown in Figure 3.2.
The Tier 1 hourly and daily TSP levels at all the ASRs are then predicted for
both scenarios of with the dust mitigation measures in place.
The ASRs identified with hourly or daily TSP non-compliance under Tier 1 screening, where mitigation measures are in place, are selected for the subsequent Tier 2 assessment.
For Tier 2 it is assumed that the percentage
active area would be located closest to the ASR being assessed. The Tier 2 hourly or daily TSP levels at each of these ASRs are
then predicted with the dust mitigation measures in place.
For the assessment of
annual TSP concentrations, the active work area over the entire year would be
less than that for a typical working hour or a typical working day. The annual TSP assessment is based on the
percentage active area. The annual TSP levels are predicted at all the ASRs for
both scenarios of with and without the dust mitigation measures in place.
To assess the operational air quality, a variety of models are required. In accordance with EPD’s Guidelines on Choice of Models and Model Parameters, the following air dispersion models have been employed to predict the cumulative pollutant concentration levels at the identified ASRs:
§ EMFAC-HKv2.5.1 (I and M) model has been used to determine the fleet average emission factors for NOx and RSP, for all the planned and existing roads within the 500m assessment area.
§ CALINE4 has been used to predict the air pollutant concentrations due to vehicular emissions from all open road links within the 500m assessment area, which are shown in Figure 3.3b.
§ ISCST3 has been used to predict the air pollutant concentrations due to stack sources at the OWTF 2
EMFAC-HKv2.5.1 is an emissions inventory model that calculates emissions inventories for motor vehicles operating on roads in Hong Kong. The model is used for estimating vehicular tailpipe emissions including RSP and NOx. The model can take into account both vehicle technologies and driving conditions. The model follows that of the California Air Resources Boards’ EMFAC model but with modifications to cater for local factors, including the substantial reduction of the smoky vehicle problem in recent years.
EMFAC-HKv2.5.1 is considered appropriate to be
used
for the impact evaluation
of this Project as
it is the most up-to-date version of the model available.
Road
Grouping
¡ Road Type A – Kong Nga Po Road (Design speed limit: 50kph);
¡ Road Type B – Man Kam To Road (Design speed limit: 50kph);
Table 3.12: Vehicle Classification in the EMFAC-HK Model
Index |
Description |
Notation in EMFAC-HK Model |
Fuel Type |
Gross Vehicle Weight |
1 |
Private Cars (PC) |
PC |
ALL |
ALL |
3 |
Taxi |
taxi |
ALL |
ALL |
4 |
Light Goods Vehicles (<=2.5t) |
LGV3 |
ALL |
<=2.5ton |
5 |
Light Goods Vehicles (2.5-3.5t) |
LGV4 |
ALL |
>2.5-3.5ton |
6 |
Light Goods Vehicles (3.5-5.5t) |
LGV6 |
ALL |
>3.5ton |
7 |
Medium & Heavy Goods Vehicles (5.5-15t) |
HGV7 |
ALL |
>5.5ton-15ton |
8 |
Medium & Heavy Goods Vehicles (>=15t) |
HGV8 |
ALL |
>15ton |
11 |
Public Light Buses |
PLB |
ALL |
ALL |
12 |
Private Light Buses (<=3.5t) |
PV4 |
ALL |
<=3.5ton |
13 |
Private Light Buses (>3.5t) |
PV5 |
ALL |
>3.5ton |
14 |
Non-franchised Buses (<6.4t) |
NFB6 |
ALL |
<=6.4ton |
15 |
Non-franchised Buses (6.4-15t) |
NFB7 |
ALL |
>6.4ton – 15ton |
16 |
Non-franchised Buses (>15t) |
NFB8 |
ALL |
<=15ton |
17 |
Single Deck Franchised Buses |
FBSD |
ALL |
ALL |
18 |
Double Deck Franchised Buses |
FBDD |
ALL |
ALL |
19 |
Motor Cycles |
MC |
ALL |
ALL |
Data was provided from the traffic consultants for current traffic flow based on measured traffic data in 2012. Twelve vehicle classes, namely: Motorcycle (MC); Private Car (PC); Taxi (TAXI); Light Goods Vehicle (LGV); Medium Goods Vehicle (MGV); Heavy Goods Vehicle (HGV); Container (CONT); Green Mini Bus (GMB); Public Light Bus (PLB); Light Bus (L BUS); Bus (BUS), and; Coach (NFB) as provided, were regrouped to the 16 vehicles classes as described in Table 3.12. Based on the vehicle population as predicted by EMFAC‑HKv2.5.1 in the year 2017, the proposed vehicle composition used for splitting the 12 vehicle classes into the 16 vehicle classes as required by EMFAC-HKv2.5.1 is shown in Table 3.13 and Appendix 3.4.
Table 3.13: Breakdown percentage of splitting 12 vehicle classes into
EMFAC-HKv2.5.1 defined vehicle classes
EMFAC vehicle
class |
Fuel Type |
MC |
PC |
TAXI |
LGV |
MGV |
HGV |
CONT |
GMB |
PLB |
L BUS |
BUS |
NFB |
PC |
Petrol |
0 |
0.996 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0.004 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
Taxi |
Petrol |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
1.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
LGV3 |
Petrol |
0 |
0 |
0 |
0.002 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0.014 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
LGV4 |
Petrol |
0 |
0 |
0 |
0.014 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0.603 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
LGV6 |
Petrol |
0 |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0.366 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
HGV7 |
Petrol |
0 |
0 |
0 |
0 |
0.000 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
1.000 |
0.261 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0.000 |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
HGV8 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0.000 |
0.000 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0.739 |
1.000 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0.000 |
0.000 |
0 |
0 |
0 |
0 |
0 |
PLB |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0.000 |
0 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.217 |
0.217 |
0 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.783 |
0.783 |
0 |
0 |
0 |
PV4 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.489 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.057 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0 |
0 |
PV5 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.002 |
0 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.207 |
0 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.245 |
0 |
0 |
NFB6 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.409 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
NFB7 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.293 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
NFB8 |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.298 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
FBSD |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.066 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0 |
FBDD |
Petrol |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0 |
|
Diesel |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.934 |
0 |
|
LPG |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0.000 |
0 |
MC |
Petrol |
1.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
Diesel |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
|
LPG |
0.000 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
0 |
Total |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
1.000 |
Exhaust / Evaporation Technology Fraction
Vehicle
Kilometres Travelled (VKT)
For each vehicle class, the Vehicle Kilometres Travelled (VKT) of both AM and PM peak hours is calculated by multiplying the hourly number of vehicles with the length of the corresponding road link (in kilometres). The AM and PM peak traffic pattern for the observed data in 2012 was given by the traffic consultant.
The 2012 traffic pattern and Annual Traffic Census data was used to project the AM and PM peak flows for operation year 2017. Traffic information for Kong Nga Po Road was measured in the Annual Traffic Census in years 2004, 2005, 2009 and 2010. Based on this information an average growth of 1.8% per year was calculated. The growth factor of 1.8% was applied to the observed 2012 data to estimate the AM and PM total traffic count for 2017.
Individual growth factors were applied to the various vehicle classes based on the measured traffic population in the Annual Traffic Census for 2002 to 2011. Motorcycles and Private Vehicles were expected to grow by 2.5%pa, Taxis, Franchised Buses, Public Light Buses and Goods Vehicles were expected to grow by 0%pa and Non-franchised Buses were expected to grow by 0.4%pa. Full calculation details can be found in Appendix 3.6.
Additional
traffic is expected to occur south of the Kong Nga Po / Man Kam
To Road intersection due to the OWTF 2 project. The
portion of Man Kam To Road
that lies within the study area is to the north of this junction; therefore, no
additional traffic due to the OWTF 2 is expected at this portion.
During operation phase of the OWTF 2, it is
anticipated that extra traffic flows will be generated mainly at the Kong Nga
Po Road and the associated AM and PM peak-hour flows will be increased by 31 pcu/h and 30 pcu/h respectively. The vehicles
travel approximately 590 m of Kong Nga Po Road, within the assessment area to
reach the OWTF 2 site. All additional traffic flows are assumed to be heavy
goods vehicles (HGV). A conservative conversion factor of 2 pcu/veh has been applied to determine the additional HGV
emissions generated by OWTF 2 (where 2 pcu/veh for Medium Goods Vehicles, 2.5 pcu/veh for Heavy Goods Vehicles), giving additional traffic
volumes of 15 veh/hr and 16
veh/hr for AM and PM
peak-hour flows respectively. Total traffic flowrates for 2017 including vehicle class are in Appendix 3.7. The sections of Kong Nga Po Road and Man Kam To Road within the project
boundary are 1428 m and 998 m respectively.
The number of trips in the assessment area, Trip within
assessment area, has been estimated as:
Trip within assessment area = (Trip within
HK/VKT within HK) x VKT within assessment
area
While the number of trips is dependent on vehicle population, project-specific vehicle population data is not available for the assessment area. However, project-specific VKT has been estimated based on the traffic forecast in the assessment area. Moreover, it can be argued that VKT is related to vehicle population in such a way that a higher vehicle population would generally result in a higher VKT. As a result, the number of trips in the assessment area has been estimated on the basis of the project-specific VKT and the assumption that the number of trips per VKT in the assessment area would be similar to the number of trips per VKT in Hong Kong. This approach for estimating the number of trips is a commonly used and accepted method and is based on reasonable assumptions and the best available data.
Hourly
Temperature and Relative Humidity Profile
Speed fraction data was not available for
the observed data from the 2012 traffic survey carried out as part of the TIA.
The speed limit for both Kong Nga Po Road and Man Kam
To Road is 50 km/h. The TIA shows the intersection at
Kong Nga Po and Man Kam To
Road is predicted to still have operating capacity in 2022. From this it is
assumed that there is no congestion on the roads and therefore traffic is able
to travel at the road design speed of 50 km/h.
Predicted
Emission Factors by EMFAC-HKv2.5.1 model
As limited data is available for this assessment, emission rates were modelled for year 2017 only. In modelling with EMFAC-HKv2.5.1, the emissions for each vehicle class at the AM and PM peak hours are then divided by the corresponding VKT to obtain emission factors in grams/vehicle-kilometre (g/veh-km). The calculations of emission factors are shown in Appendix 3.11. Despite only running for a single year it is considered that the worst-case emission values are used for the calculation. This is because despite the increased traffic volume, the total emissions are expected to decrease as a result of the retirement of older and more polluting vehicles in the fleet, which would be replaced with newer vehicles with lower emissions, this pattern is commonly shown (refer to EIA 210/2013 Table 3.8, EIA 209/2013 Table 5.12, EIA 208/2013 Table 4.28). Therefore, the emission factors for the prediction of air quality impacts due to vehicular emissions in 2017 are considered to be conservative.
In accordance with EPD’s Guidelines on Choice of Models and
Model Parameters, the Industrial Source Complex – Short Term version 3
(ISCST3) model was used to quantitatively assess the air quality impact due to
the following key emission sources:
¡ Stack exhaust for CHP (Point source);
¡ Flare exhaust (Point Source);
¡ Exhaust from odour treatment unit (Point source).
ISCST3 is a steady state Gaussian plume model which can be used to assess pollutant concentrations from sources associated with an industrial source complex. ISCST3 and all Gaussian based dispersion models have limited ability to predict dispersion in the situations as described previously in Section 3.6.1.2.
The operational sources for ISCST3 modelling (shown in Figure 3.3a and 3.3b) include:
Stack
exhaust for CHP
To allow for the greatest flexibility in the design and tender stage and to predict the reasonable worst case, the maximum concentrations from both OWTF 1 and OWTF 2 have been chosen. Modelled emissions are in Table 3.8.
Exhaust
from odour treatment unit
To allow for the greatest flexibility in the design and tender stage and to predict the reasonable worst case, the maximum concentrations from both OWTF 1 and OWTF 2 have been chosen. Modelled emissions are shown in Table 3.9.
Flare
exhausts
No emissions information for OWTF 2 was available for the flare at the time of assessment; it is therefore assumed that the emissions would be the same as those in OWTF 1. These values are considered to be reasonable as the processes and feedstocks are similar. Modelled emissions are shown in Table 3.10.
Background
concentrations and meteorological data
PATH background concentrations of the relevant pollutants (NO2, RSP, SO2) for year 2020 and TSP background level of 67 µg/m³, which is the 5-year average TSP levels recorded in EPD’s Tai Po Air Quality Monitoring Station (see Table 3.5) have been added to the modelled values. The hourly, daily and annual pollutant concentrations at the identified ASRs have been predicted and compared with the hourly, daily and annual average AQOs.
Hourly meteorological data for a full year extracted from the most up-to-date PATH model released by EPD in December 2012 (meteorological data year 2010, grid 25, 44) has been adopted for ISCST3 as it is considered to be the most current data available and representative of the site wind data at the OWTF 2.
According the information provided by EPD (Appendix 3.14), there is no existing/planned chimney emission (e.g., chimney for the Specified Process or chimney application under the Air Pollution Control Ordinance) within the 500 m study area of the Project site. Therefore, no other point sources would be included in the ISCST3 modelling.
The PATH model is a numerical air quality modelling system developed specifically for use in Hong Kong. The model comprises of three models: an emission model; a prognostic meteorological model; and a Eulerian transport and chemistry model. These models are interfaced together and set up on a series of nested domains to account for influences outside of Hong Kong and are used to predict regional wide background pollution concentrations.
An
updated version of PATH was released by the EPD for general use in December
2012. As there is no inventory update since the release of the latest PATH, for
the submission of this report, use of the 2012 PATH model in its current state
is considered appropriate.
NOx
to NO2 Conversion
The
Ozone Limiting Method (OLM) as described in EPD’s Guidelines on Choice of
Models and Model Parameters has been adopted to estimate the conversion
of NOx to NO2 from vehicular
emissions and for NOx emissions on site
from burning of biogas. A conversion factor of 0.1 of NOx
to NO2 for biogas burning has been adopted as was used in OWTF 1
assessment. The ozone concentrations are based on the future hourly background
ozone concentrations for year 2020, which were extracted from grid (25, 44) of
the most up to date PATH. The total NO2 is therefore estimated as
follows:
[NO2]total = 0.10 x [NOx]ISC
+ minimum of {0.90 x [NOx]ISC
or (46/48) x [O3]PATH} + 0.075 x [NOx]vehicle
+ minimum of {0.925 x [NOx]vehicle
or (46/48) x [O3]PATH}+ [NO2]PATH
where
¡ [NO2]total is the total hourly NO2
concentration;
¡ [NOx]ISC
is the hourly NOx concentration as predicted by ISCST3;
¡ [NOx]vehicle the
hourly NOx concentration as predicted by
Caline4;
¡ [NO2]PATH is the hourly NO2
concentrations as extracted from the aforementioned grid of
the PATH model.
Similarly,
the other total hourly concentrations are also calculated by adding together
the hourly results predicted by ISCST3 and PATH concentration.
With
the total hourly concentration estimated, the daily results are obtained by
taking the arithmetic mean of the 24 hourly results. Similarly, the annual
concentrations are calculated as the arithmetic mean of the whole year of
hourly results.
RSP
to FSP Conversion
The
conversion of RSP to FSP has been described in EPD’s Guidelines on the Estimation of PM2.5 for Air Quality Assessment
in Hong Kong. Background FSP emissions were estimated by applying a
multiplication factor of 0.75 to the background RSP from PATH. The nearfield emissions of FSP were estimated by running the
EMFACv2.5.1 model for FSP. The ratio of FSP:RSP was
found to be 0.92:1. This information was used as a conversion factor to
calculate the FSP concentrations from vehicular emissions. Calculations are
shown in Appendix
3.11. No information was available for the FSP:RSP ratio for the OWTF equipment, including emissions from
flaring and from the CHP. A conservative assumption of 100% of RSP from flaring
or the CHP unit is used for FSP emissions for these units.
Odour Conversion
In Approved Methods for the Modelling and
Assessment of Air Pollutants in New South Wales, Department of Environment and
Conservation (NSW) peak-to-mean ratios are used to convert mean 1-hour
averages to peak 1-second averages. The value for wake-affected point sources
of 2.3 (for all stability classes) has been used to predict 5-second average
concentrations. It should be noted the peak-to-mean ratios are for flat terrain
and may over or under predict the values at the ASRs.
Operation of the Project is expected to commence in 2017. Based
on current available information, the proposed/committed projects that are
anticipated to have cumulative effects during the operation phase of the
Project include:
¡ Cement Plant and the proposed Man Kam To Development Corridor; and
¡ Columbarium, Crematorium and related facilities at Sandy Ridge Cemetery recommended in the “Land Use Planning for the Closed Area Feasibility Study”..
Projects
identified are in early development (recommended or feasibility) and there is
currently no information regarding the development program or emissions these
projects may produce. Therefore, they are not assessed in this EIA and would
need to be included in studies conducted by the project proponent.. There are no planned/existing chimneys within the study
area.
The Tier 1 screening results for mitigated
scenarios including the background contribution are summarised in Table 3.14. The full results can be found in Appendix
3.12. There
are no ASRs that exceed the hourly TSP criterion, the daily or annual TSP AQOs
for the Tier 1 mitigated scenario. Therefore it is not necessary to model the
Tier 2 scenario. The contours for hourly, daily and annual unmitigated and
mitigated concentrations are shown in Figures
3.4a to 3.4f.
Table 3.14: Construction modelling results summary (Tier 1 mitigated scenario)
Pollutant |
Averaging Period |
Current Criteria (µg/m3) |
Maximum concentration range for all ASR (µg/m3) |
Total Suspended Particulate (TSP) |
1 hour |
500 |
86 to 421 |
24 hour |
260 |
70 to 128 |
|
Annual |
80 |
68 to 79 |
The operational phase assumes digester heights of 25 m, stack height of 30 m and flare height of 20 m. The rest of the major buildings and facilities are between 11 to 19 m. The emissions modelled are for mitigated values as shown in Table 3.8 and Table 3.9.
The pollutants assessed were:
¡ Nitrogen dioxide (NO2);
¡ Respirable Suspended Particulate (RSP/PM10);
¡ Fine Suspended Particulate (FSP/PM2.5);
¡ Total Suspended Particulate (TSP/Dust);
¡ Carbon Monoxide (CO);
¡ Sulfur Dioxide (SO2);
¡ Odour;
¡ Volatile Organic Compounds (VOC);
¡ Hydrogen Chloride (HCl), and;
¡ Hydrogen Fluoride (HF).
Table 3.15 summarises
the cumulative operational modelling results against the AQO as of January
2013. Full results can be found in Appendix 3.13.
Shaded cells indicate the modelled value is above the existing AQO and the
allowable exceedances, that is, the modelled value is
non-compliant. The contours of the operational scenarios are shown in Figure
3.6 to Figure
3.41.
The modelling results show that the predicted maximum concentrations of various
air pollutants at all ASRs are compliant with the current AQOs.
Table 3.15: Cumulative operation modelling results summary (Mitigated)
Pollutant |
Averaging Period |
Current AQO (µg/m3) |
Maximum concentration range for all ASR (µg/m3) |
Nitrogen dioxide (NO2) |
1 hour |
300 |
155.0 to 187.3 |
24 hour |
150 |
78.4 to 92.3 |
|
Annual |
80 |
20.5 to 29.1 |
|
Respirable Suspended Particulate (RSP/PM10) |
24 hour |
180 |
121.0 to 126.9 |
Annual |
55 |
43.0 to 43.6 |
|
Total Suspended Particulate (TSP/Dust) |
1 hour |
500(1) |
68.0 to 206.3 |
24 hour |
260 |
68.0 to 89.0 |
|
Annual |
80 |
68.0 to 68.9 |
|
Carbon Monoxide (CO) |
1 hour |
30,000 |
2278.1 to 2280.4 |
8 hour |
10,000 |
1458.7 to 1461.3 |
|
Sulfur Dioxide (SO2) |
1 hour |
800 |
65.9 to 66.7 |
24 hour |
350 |
27.1 to 27.9 |
|
Annual |
80 |
6.5 to 6.6 |
|
Odour |
5 second |
5(2) |
0.00 to 1.59 |
Volatile Organic Compounds (VOC) |
1 hour |
60000(3) |
2.5 to 9423.2 |
Hydrogen Chloride (HCl) |
1 hour |
2100(3) |
0.3 to 5.8 |
Annual |
20(3) |
0.001 to 0.031 |
|
Hydrogen Fluoride (HF) |
1 hour |
240(3) |
0.00 to 0.58 |
Annual |
14(3) |
0.0001 to 0.0031 |
2. Unit is OU/m3
3. Refer
to Table
3.3
Table 3.16 summarises the cumulative operational
modelling results against the AQO as of January 2014. Full results can be found
in Appendix 3.13. Shaded cells indicate the modelled value
is above the new AQO and the allowable exceedances,
that is, the modelled value is non-compliant. The modelling results show that
the predicted maximum concentrations of various air pollutants at all ASRs are
compliant with the new AQOs.
Table 3.16: Cumulative operation modelling results summary (Mitigated)
Pollutant |
Averaging Period |
New AQO (µg/m3) |
Maximum concentration range
for all ASR (µg/m3) |
Nitrogen dioxide (NO2) |
1 hour |
200 |
155.0 to 187.3 |
Annual |
40 |
20.5 to 29.1 |
|
Respirable Suspended Particulate (RSP/PM10) |
24 hour |
100 |
121.0
to 126.9(4) |
Annual |
50 |
43.0 to 43.6 |
|
Fine Suspended Particulate (FSP/PM2.5) |
24 hour |
75 |
90.7 to 96.6(4) |
Annual |
35 |
32.3 to 32.8 |
|
Total Suspended Particulate (TSP/Dust) |
1 hour |
500(1) |
68.0 to 206.3 |
Carbon Monoxide (CO) |
1 hour |
30,000 |
2278.1 to 2280.4 |
8 hour |
10,000 |
1458.7 to 1461.3 |
|
Sulfur Dioxide (SO2) |
10 minute |
500 |
161.5 to 163.3 |
24 hour |
125 |
27.1 to 27.9 |
|
Odour |
5 second |
5(2) |
0.00 to 1.59 |
Volatile Organic Compounds (VOC) |
1 hour |
60000(3) |
2.5 to 9423.2 |
Hydrogen Chloride (HCl) |
1 hour |
2100(3) |
0.3 to 5.8 |
Annual |
20(3) |
0.001 to 0.031 |
|
Hydrogen Fluoride (HF) |
1 hour |
240(3) |
0.00 to 0.58 |
Annual |
14(3) |
0.0001 to 0.0031 |
1. TM-EIAO
2. Unit is OU/m3
3. Refer to Table 3.3
4. Maximum
predicted exceedance for all ASR is 2 per year.
Maximum allowable exceedances per year is 9. Therefore, 24 hour average RSP and FSP
are compliant
To achieve compliance with the TSP criteria
during the construction phase, good practices for dust control should be
implemented to reduce dust impacts. The dust control measures are detailed as
follows:
Dust emissions could be suppressed by
regular water spraying on site. In general, water spraying twice a day could
reduce dust emission from active construction area by 50%. However, for OWTF 2
more frequent water spraying is proposed. Watering eight times per day, or once
every 1.5 hours, is suggested at all active works areas in order to achieve a
higher dust suppression efficiency of 87.5%. The calculation for dust
suppression by watering is in Appendix
3.3.
Construction activities include construction of roads, drilling, ground
excavation, cut and fill operations (i.e. earth
moving), etc. In addition, all
the stockpiles should be at least 80% covered with impervious sheeting to
reduce windblown dust.
In addition to implementing the recommended dust control measures mentioned above, it is recommended that the relevant best practices for dust control as stipulated in the Air Pollution Control (Construction Dust) Regulation should also be adopted to further reduce the construction dust impacts of the Project. These best practices include:
Good Site Management
¡ Good site management is important to help reducing potential air quality impact down to an acceptable level. As a general guide, the Contractor should maintain a high standard of housekeeping to prevent emissions of fugitive dust. Loading, unloading, handling and storage of raw materials, wastes or by-products should be carried out in a manner so as to minimise the release of visible dust emission. Any piles of materials accumulated on or around the work areas should be cleaned up regularly. Cleaning, repair and maintenance of all plant facilities within the work areas should be carried out in a manner minimising generation of fugitive dust emissions. The material should be handled properly to prevent fugitive dust emission before cleaning.
Disturbed Parts of the Roads
¡ Each and every main temporary access should be paved with concrete, bituminous hardcore materials or metal plates and kept clear of dusty materials; or
¡ Unpaved parts of the road should be sprayed with water or a dust suppression chemical so as to keep the entire road surface wet.
Exposed Earth
¡ Exposed earth should be properly treated by compaction, hydroseeding, vegetation planting or seating with latex, vinyl, bitumen within six months after the last construction activity on the site or part of the site where the exposed earth lies.
Loading, Unloading or Transfer of Dusty Materials
¡ All dusty materials should be sprayed with water immediately prior to any loading or transfer operation so as to keep the dusty material wet.
Debris Handling
¡ Any debris should be covered entirely by impervious sheeting or stored in a debris collection area sheltered on the top and the three sides.
¡ Before debris is dumped into a chute, water should be sprayed so that it remains wet when it is dumped.
Transport of Dusty Materials
¡ Vehicle used for transporting dusty materials/spoil should be covered with tarpaulin or similar material. The cover should extend over the edges of the sides and tailboards.
Wheel washing
¡ Vehicle wheel washing facilities should be provided at each construction site exit. Immediately before leaving the construction site, every vehicle should be washed to remove any dusty materials from its body and wheels.
Use of vehicles
¡ The speed of the trucks within the site should be controlled to about 10km/hour in order to reduce adverse dust impacts and secure the safe movement around the site.
¡ Immediately before leaving the construction site, every vehicle should be washed to remove any dusty materials from its body and wheels.
¡ Where a vehicle leaving the construction site is carrying a load of dusty materials, the load should be covered entirely by clean impervious sheeting to ensure that the dusty materials do not leak from the vehicle.
Site hoarding
¡ Where a site boundary adjoins a road, street, service lane or other area accessible to the public, hoarding of not less than 2.4m high from ground level should be provided along the entire length of that portion of the site boundary except for a site entrance or exit.
The modelling results are based on mitigated emissions from the various equipment and all ASRs have been found to be within the relevant existing AQO criteria for all assessed air quality pollutants. The mitigation measures suggested for the operation phase are to include gas cleaning equipment and stack on the CHP and odour treatment unit.
The
preliminary design suggests the use of a two stage process involving either a biofilter or Ultraviolet Light (UV-C) together with ozone
treatment as the first stage, and an activated carbon filter as the second
stage for the odour treatment unit. It is
recommended to install the UV-C and ozone treatment system with second stage
active carbon filters as this has a lower footprint requirement than the biofilter option. Based on the untreated odour emission
strength on 500 ou/m3 and flowrate of 195,000 m3/hr,
a minimum odour removal efficiency of 90% is recommended to give a maximum
outlet emission concentration of 50 ou/m3.
However, the actual unit installed depends on
the final design by the contractor in the design phase.
For the CHP, the preliminary design incorporates a combination of thermal and catalytic treatment processes to remove pollutants from the exhaust gasses from the CHP.
Both the odour treatment unit and the CHP emissions are suggested to be directed to a flue to aid the dispersion and minimise effects on ASRs.
RCV’s travelling to and from the OWTF2 site must be clean and the waste transfer compartment sealed during transport to avoid odour impacts. Deliveries will be scheduled to minimise / avoid queuing of vehicles [8]. In parallel, OWTF2 operator will not wish to accumulate waste materials at the site and will facilitate prompt processing.
Waste deliveries may comprise either conventional Refuse Collection Vehicles (RCV) or vehicles transporting purpose built containers that enclose the loose or bagged organic waste. The containment unit (RCV or container) must be designed to prevent ingress of rainwater (reducing leachate generation) and leakage of leachate. The container unit must be robust and made of a corrosion resistant material (stainless steel or high density / hard wearing plastic are preferred). These container units will be sealable to ensure a water and air tight seal that prevents ingress of water or any escape of odour. Following discharge at the OWTF2 the waste transfer vehicles will pass through a cleaning process before leaving the facility to remove potential for odour impact on the public highway. In view of this, odour emission from the waste collection vehicles during transportation of organic waste is therefore not anticipated.
With proper implementation of the
recommended mitigation measures, no ASRs are predicted to exceed the hourly,
daily or annual TSP criteria, hence there are no residual effects anticipated during
the construction phase.
The project is expected to be in compliance
with the current and new AQO limits and other relevant criteria for all
pollutants assessed.
Although the project is expected to be in
compliance of the current and new AQO and other relevant criteria, it is still
recommended to apply the mitigation measures, to minimise the potential effect
on ASRs.
As no ASRs are predicted to exceed the relevant criteria with implementation of the recommended mitigation measures, regular dust monitoring is not considered necessary during the construction phase of the Project. However, regular site audits are suggested to ensure the dust control measures are properly implemented. Details of the environmental monitoring and audit (EM&A) programme will be presented in the stand-alone EM&A Manual.
Should the recommended mitigation measures be implemented for the operational phase, no ASRs are predicted to exceed the relevant criteria under the current and new AQOs. Odour patrol at the project site boundary is proposed to monitor any odour impact arising from the operation of the OWTF. Regular audits are also suggested to ensure proper operation and maintenance of the recommended pollution control equipment. Details of the environmental monitoring and audit (EM&A) programme are contained in the stand-alone EM&A Manual.
With the implementation of the recommended mitigation measures as well as the relevant control requirements as stipulated in the Air Pollution Control (Construction Dust) Regulation, it has been assessed that there would be no exceedance of the hourly, daily or annual TSP criteria at any of the ASRs.
During the operation phase, all the assessed ASRs would be in compliance with the relevant current and new AQOs and other relevant criteria for all emissions modelled in this EIA. It is recommended that emission control equipment should be installed to reduce any potential effects on the local residents and sensitive receivers.
The recommended mitigation measures include gas cleaning equipment and stack for the CHP and odour treatment unit. This odour treatment assessment is based on the application of a UV-C and ozone treatment system with second stage active carbon filters recommended in the preliminary design. For the CHP, the preliminary design incorporates a combination of thermal and catalytic treatment processes to remove pollutants from the exhaust gasses from the CHP. Both the odour treatment unit and the CHP emissions are suggested to be directed to a flue to aid the dispersion and minimise effects on ASRs.
[1] TD letter to MM
ref: NR 157/161-FSSDD89 dated 25 July 2013.
[2] The Traffic
Impact Assessment for the OWTF 2 assumes an average of 60 Refuse Collection
Vehicles (RCV) each day with a conservative allowance for 10 RCV each day in
line with the approach adopted for OWTF1
[3] Industry good
practice includes correctly operated and maintained Refuse Collection Vehicles
(RCV) with appropriately sized leachate reservoirs and with collection chamber
sealed during transport phase or dedicated sealable containers used for transport
between collection point and OWTF2
[4]
http://www.epd-asg.gov.hk/english/report/files/AQR2011e_final.pdf
[5]
http://www.epd-asg.gov.hk/english/report/files/AQR2012_prelim_en.pdf
[6] Winges, 1991. User’s Guide for the Fugitive Dust Model
(FDM) (Revised) User’s Instructions. Seattle, USEPA.
[7] Good Practice
Guide for Atmospheric Dispersion Modelling. Ministry for the Environment, New Zealand (June 2004)
[8] It is not in waste collection operators commercial interests to
have vehicles queuing to discharge loads at OWTF2 as this is non-productive
time, Operators will arrange their schedules to minimise
queue times at OWTF2.