6
WATER POLLUTION
6.1
Introduction
6.1.1.1
This section presents
an assessment of the potential water quality impacts associated with the construction
and operation phases of the proposed STF. Recommendations for mitigation
measures have been made, where necessary, to reduce the identified water
quality impacts to an acceptable level.
6.2
Environmental Legislation and Standards
6.2.1
Water Pollution Control Ordinance (WPCO)
6.2.1.1
The Water Pollution
Control Ordinance (Cap. 358) is the major legislation relating to the
protection and control of water quality in Hong Kong.
According to the Ordinance and its subsidiary legislation, Hong
Kong waters are divided into ten water control zones (WCZ).
Corresponding statements of Water Quality Objectives (WQO) are stipulated for
different water regimes (marine waters, inland waters, bathing beaches
subzones, secondary contact recreation subzones and fish culture subzones) in
the WCZ based on their beneficial uses. The study area is located within
the Deep Bay WCZ and the corresponding WQO are listed in Table 6.1.
Table 6.1
Summary of Water Quality Objectives for Coastal Waters of Deep Bay Water
Control Zone
Parameter
|
Objective
|
Part(s) of Zone
|
E. coli
|
annual
geometric mean not to exceed 610 cfu/100 ml
|
secondary contact recreation
subzone
mariculture subzone
|
Dissolved Oxygen within 2 m of bottom
|
not less
than 2 mg/L for 90% samples
|
|
Depth averaged dissolved oxygen
|
not less
than 4 mg/L for 90% samples
|
Dissolved Oxygen at 1 m below surface
|
not less
than 4 mg/L for 90% samples
|
inner marine subzone except mariculture subzone
|
pH value
|
within the range 6.5 to 8.5; change due to
waste discharge not to exceed 0.2
|
marine waters
|
Salinity
|
change due
to waste discharge not to exceed 10% of natural ambient level
|
whole zone
|
Temperature
|
change due
to waste discharge not to exceed 2oC
|
whole zone
|
Suspended solids
|
waste
discharge not to raise the natural ambient level by 30%, nor cause the
accumulation of suspended solids which may adversely affect aquatic
communities
|
marine waters
|
Nutrients
|
not to be present in quantities that cause excessive growth of algae
or other aquatic plants
|
Inner and outer marine
subzones
|
annual mean depth-averaged inorganic nitrogen not to exceed 0.5 mg/L
|
Outer marine subzone
|
annual mean depth-averaged inorganic nitrogen not to exceed 0.7 mg/L
|
Inner marine subzone
|
Unionized Ammonia
|
annual average should not exceed 0.021 mg/L
|
whole zone
|
6.2.2
Technical Memorandum
6.2.2.1
Besides setting the WQOs, the WPCO controls effluent discharging into the WCZs through a licensing system. A Technical
Memorandum (TM) on Standards for Effluents Discharged into Drainage and
Sewerage Systems, Inland and Coastal Waters has been issued under the WPCO
which gives guidance on the permissible effluent discharges based on the type
of receiving waters (foul sewers, storm water drains, inland and coastal
waters). The limits control the physical, chemical and microbial quality
of effluents. Any effluent discharges during the construction and
operational stages should comply with the standards for effluents discharged
into the coastal waters of the Deep Bay WCZ, as shown in Table 8 of the TM.
6.2.2.2
In addition to the
provisions of the TM, the ‘No Net Increase Requirement in Pollution Loading’
aims to provide protection to the inland and marine water quality of the Deep
Bay WCZ. The policy requires that developments within the Deep Bay
catchment areas do not result in an increase in pollution loads to the inland
and marine waters.
6.2.3
Practice Notes
6.2.3.1
A practice note (PN)
for professional persons has been issued by the EPD to provide environmental
guidelines for handling and disposal of construction site discharges. The
ProPECC PN 1/94 “Construction Site Drainage”
provides good practice guidelines for dealing with various types of discharge
from a construction site. Practices outlined in the PN should be followed
as far as possible during construction to minimize the water quality impact due
to construction site drainage.
6.3
Baseline Conditions
6.3.1
Inland Waters
6.3.1.1
The construction of the
STF and the associated access road has the potential to affect the inland watercourse
of Tsang Kok stream within the Deep Bay WCZ.
There is one EPD routine water quality monitoring station (DB8) along the Tsang
Kok Stream (see Figure 6.1). A summary of the
published monitoring data (in 2006) for this station is presented in Table 6.2.
Table 6.2
Summary of Water Quality Monitoring Results for Tsang Kok
Stream in 2006
Parameter
|
Unit
|
DB8
|
Dissolved oxygen
|
mg/L
|
9.5
(7.4 – 10.9)
|
pH
|
-
|
7.9
(6.5 – 9.0)
|
Suspended solids
|
mg/L
|
4
(2 – 88)
|
5-day
Biochemical Oxygen Demand
|
mg/L
|
1
(1 – 2)
|
Chemical Oxygen Demand
|
mg/L
|
4
(2 – 9)
|
Oil & grease
|
mg/L
|
0.5
(0.5 – 0.5)
|
Faecal coliforms
|
cfu/100mL
|
5400
(1900 – 17000)
|
E.coli
|
cfu/100mL
|
310
(31 – 3600)
|
Ammonia-nitrogen
|
mg/L
|
0.02
(0.01 – 0.08)
|
Nitrate-nitrogen
|
mg/L
|
0.25
(0.09 – 0.98)
|
Total Kjeldahl
nitrogen, SP
|
mg/L
|
0.12
(0.06 – 0.35)
|
Ortho-phosphate
|
mg/L
|
0.01
(0.01 – 0.02)
|
Total phosphorus, SP
|
mg/L
|
0.02
(0.02 – 0.03)
|
Sulphide, SP
|
mg/L
|
0.02
(0.02 – 0.08)
|
Aluminium
|
µg/L
|
120
(50 – 290)
|
Cadmium
|
µg/L
|
0.1
(0.1 – 0.1)
|
Chromium
|
µg/L
|
1
(1 – 1)
|
Copper
|
µg/L
|
1
(1 – 2)
|
Lead
|
µg/L
|
1
(1 – 20)
|
Zinc
|
µg/L
|
10
(10 – 20)
|
Flow
|
L/s
|
NM
|
Notes:
1.
Data
presented are in annual medians of monthly samples, except those for faecal coliforms and E.coli which
are in annual geometric means. Figures in brackets are annual ranges.
2.
SP – soluble
and particulate fractions (i.e. total value).
3.
NM
indicates no measurement taken
6.3.1.2
River water quality
monitoring data for the year 2006 at station DB8 showed the overall compliance
rate of the Tsang Kok stream with the WQOs was 100%, with full compliance with the WQOs of pH, suspended solids, dissolved oxygen, COD and BOD5.
The water quality of this minor stream was reported to be excellent and
free from point source pollution.
6.3.1.3
A description of the
physical characteristics of the stream course is presented under the ecological
section in Section 7.
6.3.2
Marine Waters
6.3.2.1
The EPD water quality
monitoring station DM4 in the Deep Bay WCZ is the nearest monitoring station in
the vicinity of the Project area (see Figure
6.1). A summary of the published monitoring data (in 2006) for
this station is presented in Table 6.3.
Table 6.3
Summary Statistics of Marine Water Quality in the Deep Bay WCZ at Station DM4
Parameter
|
EPD Monitoring Station DM4
|
Water Quality
Objectives
(in marine
waters)
|
Temperature
(oC)
|
24.7
(19.2 – 29.3)
|
Natural daily
level ± 2 oC
|
Salinity
(ppt)
|
23.9
(14.2 – 30.8)
|
natural ambient
level ± 10 %
|
Dissolved Oxygen (DO)
(mg L-1)
|
5.7
(4.0 – 6.6)
|
³ 4 mg L-1
|
Dissolved Oxygen (DO) –
Bottom (mg L-1)
|
5.6
(3.8 – 6.7)
|
³ 2 mg L-1
|
DO
(% saturation)
|
78
(57 – 85)
|
-
|
DO –Bottom
(% saturation)
|
77
(55 – 88)
|
-
|
pH value
|
7.6
(7.2 – 8.1)
|
6.5 - 8.5 (± 0.2 from natural
range)
|
Secchi disc
(m)
|
0.5
(0.2 – 1.2)
|
-
|
Turbidity
(NTU)
|
19.5
(11.0 – 33.0)
|
-
|
SS
(mg L-1)
|
13.5
(3.0 – 35.1)
|
£ natural ambient
level + 30%
|
Silica (as SiO2)
(mg L-1)
|
2.8
(0.7 – 6.3)
|
-
|
BOD5
(mg L-1)
|
0.9
(0.3 – 1.5)
|
-
|
Nitrite Nitrogen
(mg L-1)
|
0.138
(0.096 – 0.215)
|
-
|
Nitrate Nitrogen
(mg L-1)
|
0.54
(0.25 – 0.99)
|
-
|
Ammonia Nitrogen
(mg L-1)
|
0.41
(0.19 – 0.76)
|
-
|
Unionised Ammonia
(mg L-1)
|
0.009
(0.002 – 0.016)
|
£ 0.021 mg L-1
|
Total Inorganic Nitrogen
(mg L-1)
|
1.10
(0.80 – 1.40)
|
£ 0.5
mg L-1
|
Total Kjeldahl Nitrogen
(mg L-1)
|
0.64
(0.43 – 0.96)
|
-
|
Total Nitrogen
(mg L-1)
|
1.30
(0.96 – 1.69)
|
-
|
Orthophosphate Phosphorus
(mg L-1)
|
0.06
(0.02 – 0.09)
|
-
|
Total Phosphorus
(mg L-1)
|
0.08
(0.05 – 0.11)
|
-
|
Chlorophyll-a
(µg L-1)
|
3.84
(1.0 – 13.0)
|
-
|
E. coli
(cfu
per 100 mL)
|
740
(150 – 2900)
|
< 610 cfu per 100 mL
|
Faecal Coliform
(cfu
per 100 mL)
|
1400
(270 – 4100)
|
-
|
Notes:
1.
Data
source: EPD (2006). Marine Water Quality In Hong Kong in 2006.
2.
Except as specified, data presented are depth-averaged data.
3.
Data
presented are arithmetic means except for E. coli and faecal coliforms that are geometric means.
4.
Data
enclosed in brackets indicate ranges.
6.3.2.2
According to the “2006
Marine Water Quality in Hong Kong”, water
quality monitoring data for station DM4 met the WQOs
for dissolved oxygen (bottom and depth-averaged) and unionized ammonia.
Non-compliance was recorded with the WQO for total inorganic nitrogen which was
reported to be the result of a persistent nutrient pollution problem in Deep Bay.
An increase in the level of E.coli
(annual geometric mean) was reported with non-compliance with the WQO.
6.4
Water Sensitive Receivers
6.4.1.1
Two moderate sized
streams are located near to the proposed Project site at the eastern part of
the ash lagoon area and discharge into a tidal channel to the east of the ash
lagoon area (refer to Figure 7.1).
The lower reaches of stream W1 are routed through a man-made, tidally
influenced channel to the south of the ash lagoons. Although the substrate of
this channel is natural, the banks have been lined with geo-textile
matting. The second stream (stream W2) drains into the tidal channel from
the southeast. The section of stream flowing through the existing WENT
Landfill site has been wholly channelized with concrete.
6.4.1.2
Apart from the coastal
waters of Deep Bay, no other marine sensitive receivers
within the vicinity of the Project area were identified. The STF will
adopt a “zero-discharge” scheme and no process effluent will be discharged into
Deep Bay during the operational phase.
6.5
Assessment Methodology
6.5.1.1
The Assessment Area as
specified in the EIA Study Brief covers an area within 300m of the Project site
boundary, and all relevant water sensitive receivers downstream of any
emergency bypass from the proposed sewage treatment works within STF, including
the existing cooling water system of Black Point Power Station.
6.5.1.2
The water sensitive
receivers that may be affected by the various construction activities for the
STF were identified. Potential sources of water quality impact that may
arise during the construction phase of the Project were described. This
task included identifying pollutants from point discharges and non-point
sources to surface water run-off. All the identified sources of potential
water quality impact were then evaluated and their impact significance
determined. The need for mitigation measures to reduce any identified
adverse impacts on water quality to acceptable levels was determined.
6.5.1.3
The assessment of
operational stage water quality impacts addressed the following potential areas
of concern: any proposal for on-site wastewater treatment plant(s); analysis on
the adequacy of existing and future sewerage infrastructure; any proposal for
upgrading or providing effective sewerage infrastructure; possible emission of
microbes associated with the transportation, storage and handling of dewatered
sewage sludge into surrounding waterbodies; and any
thermal discharge from cooling water system.
6.6
Identification and Evaluation of Environmental
Impacts
6.6.1
Construction Phase
6.6.1.1
Potential sources of
water quality impact associated with the construction phase of the proposed STF
have been identified and include:
l
Drainage and construction site runoff during site
formation and foundation piling;
l
General construction activities;
l
Sewage effluent produced by on-site workforce; and
l
Release of PFA leachate from
ash lagoon into the aquatic environment.
Drainage and Construction Site Runoff
6.6.1.2
Runoff from the
construction works area may contain increased loads of sediments, other
suspended solids and contaminants. Potential sources of pollution from
site drainage include:
l
Runoff and erosion from exposed soil surfaces, earth
working areas and stockpiles;
l
Release of grouting and cement materials with rain
wash;
l
Wash water from dust suppression sprays; and
l
Fuel and lubricants from maintenance of construction
vehicles and mechanical equipment.
6.6.1.3
Sediment laden runoff during
site formation works, if uncontrolled, may carry pollutants (adsorbed onto the
particle surfaces) into the nearby stream and coastal waters.
6.6.1.4
As a good site
practice, mitigation measures should be implemented to control construction
site runoff and drainage from the works areas, and to prevent runoff and
drainage water with high levels of suspended solids from entering the nearby
water bodies. With the implementation of adequate construction site
drainage and provision of sediment removal facilities as described in Section
6.7.2.1, it is anticipated that unacceptable water quality impacts would
not arise. The construction site drainage would be collected by the
temporary drainage system installed by the Contractor and then treated on-site
before discharging into the sea via silt removal facilities. Water pumped
out from foundation piling would also be discharged into the sea via silt
removal facilities. The Contractor would be required to obtain a license
from EPD for discharge to the coastal waters.
General Construction Activities
6.6.1.5
On-site construction
activities may cause water pollution as shown below:
l
Uncontrolled discharge of debris and rubbish such as
packaging, construction materials and refuse; and
l
Spillages of liquids stored on-site, such as oil,
diesel and solvents etc, are likely to result in water quality impacts if they
enter water bodies.
6.6.1.6
Good construction and
site management practices should be implemented, as detailed in Section
6.7.2.2 and Section 6.7.2.3, to ensure that litter, fuels and
solvents do not enter the nearby stream and coastal waters.
Sewage Effluent
6.6.1.7
Domestic sewage would
be generated from the workforce during the construction phase. However,
this sewage can be adequately treated by interim sewage treatment facilities,
such as portable chemical toilets, which can be installed within the construction
site. It is unlikely that sewage generated from the site would have a
significant water quality impact, provided that sewage is not discharged
directly to the stream or the public drainage system, and chemical toilets are
used and properly maintained.
Release of PFA Leachate from Ash Lagoon into
the Aquatic Environment
6.6.1.8
The proposed STF will
be located in the eastern part of the existing ash lagoon area. The ash
lagoons were constructed in the mid- to late 1980’s and were divided by bunds
into the East, Middle and West Lagoons. Since
1989, the lagoons have been used for the storage of PFA, a by-product of the
coal-burning. PFA is a fine, grey powder formed from the rock particles
contained within coal, consisting mainly of silica, alumina and iron
oxide.
6.6.1.9
The Middle and West Ash Lagoons are still used for the
storage of PFA. In 1997, China Light and Power (CLP) began
to use the Middle Lagoon as part of its water collection and conservation
system. The ash
lagoon area is underlain by marine deposits which consist of fine grained
material. Alluvium is present underneath the marine deposits.
Depths of alluvium may vary from approximately 4.0 to 19.0m. The
layer of alluvium is underlain by completely decomposed granite (CDG) with
depths ranging from approximately 3.5 to 15.2m.
6.6.1.10
There is liner, which was constructed of cementitious materials, at the bottom of the ash
lagoons. However, in view of the nature of the liner, it is highly likely
that this layer would have already been cracked / broken under the loadings
imposed by the existing ash at the lagoons.
6.6.1.11
The marine deposits in the sea wall
location have been removed prior to the sea wall construction. In order to prevent leakage of PFA leachate through the sea wall to Deep Bay,
filter layers are laid underneath the amour stone on the inner face of the sea
wall. On the seaward side of the outer sea
wall, armour stone and wave wall are provided to resist the storm effects.
6.6.1.12
During construction phase of the Project,
piling would be applied for foundation construction. The piles would
penetrate through the base of the East Lagoon to the hard granite bedrock to
support the facility and the soil layer underneath the lagoon would be
disturbed. However, the piling activities are unlikely to cause
significant changes in geological structure of the lagoon site. The
present of piles would restrict the movement of groundwater in the soil
layer. The liner underneath the East Lagoon would have already been
creaked / broken. The underground conditions at the base on the East
Lagoon are expected to be rather stable. Leakage of PFA leachate through the base of the East Lagoon to Deep Bay
after the pile construction, if any, would not be much different from the
existing condition.
6.6.1.13
To evaluate the
potential impacts of the PFA leachate to the nearby
aquatic environment, the chemical characteristics of the PFA leachate and chemical toxicity data for aquatic life have
been reviewed. The PFA leaching trial using seawater was conducted by
Scott Wilson Kirkpatrick (1991).
The leaching trial result showed that the metals contents in the PFA
varied with the type of coal and the length of PFA aging. Only low
concentrations of potential contaminants were leached into seawater
solution. The contaminants with the greatest tendency to leach into solution
were found to be cadmium, chromium and aluminium. Fresh PFA tended to
leach more metals compared to the lagooned PFA and
was more variable among various coal types. Results from the lagooned PFA showed smaller variations and metal leaching
was more consistent.
6.6.1.14
Table 6.4 shows the concentrations of different
parameters from the lagooned PFA leaching trials.
The major heavy metals released from the lagooned
PFA were aluminium and chromium, with maximum concentrations of 900 and 300 mg/l respectively. The maximum
cadmium concentration measured in the leaching trials was 4 mg/l. There was an uncertainty
of the actual concentration of copper and nickel released from lagooned because of the high reporting limits. The
analytical instrument for the seawater solution in the leaching trials was only
available to detect copper concentration higher than 75mg/l and nickel higher than 25mg/l.
Table 6.4
Comparison of Leaching Trial Results with the Background Levels and USEPA Water
Quality Standards
Parameter
|
Leaching
Trial Results (mg/l)
|
Background
Concentration
(mg/l) Note 1
|
USEPA
Water Quality Standard for Saltwater (mg/l)
|
Aluminium
|
900
|
132
|
n/a
|
Chromium
|
300
|
1.5
|
50 (210) Note 2
|
Cadmium
|
4
|
< 0.05
|
9.3
|
Copper
|
<75
|
< 5
|
2.9
|
Zinc
|
30
|
6
|
86
|
Nickel
|
<25
|
< 5
|
8.3
|
Iron
|
20
|
145
|
n/a
|
Lead
|
6
|
0.9
|
8.5
|
Manganese
|
3
|
17.5
|
n/a
|
Selenium
|
14
|
< 1
|
71
|
Arsenic
|
3
|
1.2
|
36
|
Notes:
1.
The background concentrations were based
on the results measured around Black Point and Tap Shek
Kok abstracted from Scientific Series, Chemical
Analysis Report 20/91
2.
The value of 50 mg/l represents the standard for Chromium (VI) in
saltwater and there is no standard for Chromium (III) in saltwater. The
criterion for Chromium (III) in freshwater is 210 mg/l.
6.6.1.15
Table 6.4 also provided the concentration of trace metals measured around Black
Point and Tap Shek Kok in 1991
as background concentration, as well as USEPA Water Quality Standards for
Saltwater. Concentrations for aluminium, iron and manganese are not
available in the USEPA standard. Comparison result of the leaching trial
of these three parameters with the background concentration presented that both
iron and manganese were below the background concentration, whiles aluminium
concentration is about 7 times higher than background concentration. When
diluted by the ambient seawater, the aluminium concentration would be
indistinguishable from the background level within a short distance from the
release point.
6.6.1.16
To compare other parameters with the
USEPA standard, the concentrations of all metals except chromium are below the
USEPA standards. In the event that release of PFA leachate
occurs, the potential water quality would be low. In fact, the ash would
remain in the East Lagoon and there would be no off-site disposal of ash into
the aquatic environment.
6.6.1.17
A monitoring programme was conducted by CLP between 1987 and 1988 to
monitor water quality at the location outside the Middle Lagoon. The
monitoring result is shown in Table 6.5, indicating that there
were no significant difference between the trace metal results measured outside
the Middle Lagoon and at oyster buoy and farm in Deep Bay. To compare
these monitoring results with the background concentrations of trace metals
measured around Black Point and Tap Shek Kok measured in 1991, no evidence shows that the operation of the Tsang Tsui Lagoons has caused adverse water quality impacts in
the vicinity of the lagoon site.
Table 6.5
Results of CLP monitoring programme between 1987 and 1988
Parameters
|
Monitored
Average Concentrations (mg/l)
|
Background
Concentration
(mg/l)
|
At
Location Immediately Outside the Middle Lagoon
(Sep
1988 – Jan 1989)
|
At
Oyster Buoy and Farm in Deep
Bay
(Jun
1987 – Nov 1987)
|
Cadmium
|
0.09
|
0.41
|
< 0.05
|
Copper
|
3.6
|
2.1
|
< 5
|
Lead
|
2.3
|
1
|
0.9
|
Zinc
|
7
|
23
|
6
|
Arsenic
|
< 5
|
5.1
|
1.2
|
Selenium
|
< 10
|
No data
available
|
< 1
|
6.6.1.18
Chemical
toxicity data for aquatic life have been reviewed in order to evaluate the
potential impacts of the PFA leachate. High
concentrations of heavy metals can be detrimental to aquatic life. The
effects of high concentration of metals may cause the changes in tissues,
growth rates, blood chemistry, behaviour and reproduction of aquatic organisms.
Fish can excrete
excess heavy metals but bivalves cannot regulate excess heavy metals resulting
in metal accumulation in the tissues.
6.6.1.19
There are
no relevant aquatic life criteria in Hong Kong. The USEPA Aquatic Life
Criteria (estuarine/coastal), which provide a general guide to assess the
potential risk to the environment in the presence of excess metal, is applied
to compare with the leaching trial results (as shown in Table 6.6). The parameters of aluminium, chromium, iron and manganese are
not available in the USEPA estuarine/coastal Aquatic Life Criteria.
Except the uncertainty due to the high reporting limits for copper and nickel,
most of the listed heavy metal concentrations are lower than the criteria.
Table 6.6
Comparison of the Leaching Trial Results with the USEPA Aquatic Life Criteria
Parameter
|
Leaching Trial Results
(mg/l)
|
USEPA Aquatic Life Criteria (mg/l)
|
Aluminium
|
900
|
-
|
Chromium
|
300
|
-
|
Cadmium
|
4
|
8
|
Copper
|
<75
|
2.9
|
Zinc
|
30
|
76.6
|
Nickel
|
<25
|
7.1
|
Iron
|
20
|
-
|
Lead
|
6
|
5.8
|
Manganese
|
3
|
-
|
Selenium
|
14
|
71
|
Arsenic
|
3
|
50
|
6.6.1.20
The water
quality guidelines for general saltwater aquaculture uses adopted in the New Zealand
Guidelines for Fresh and Marine Water Quality (Table
6.7)
and the UK Water Quality Standards for the Protection of Saltwater Life (Table 6.8) are also applied to compare with the leaching trial results.
Concentrations of aluminium, chromium, copper, iron and selenium are higher
than the New Zealand Guidelines, while concentrations of chromium, cadmium and
copper are higher than the UK Standards.
6.6.1.21
Dilution
for these metals could lower the concentrations to meet the New Zealand
Guidelines and the UK Standards. The estimated dilution rates are shown
in Table 6.7 and Table 6.8. In order to meet the New Zealand Guidelines, the highest
dilution rate would be >90 for aluminium. Chromium and copper would
require a dilution rate of >15 and iron and selenium require a dilution rate
of >2. To meet the requirements of the UK Standards, the highest
dilution rate is >20 for chromium, while required dilution rate for cadmium
and copper are 1.6 and 20 respectively. The nearest oyster beds at Pak Nai are approximately 3 km away from the lagoons. The
require dilutions are likely to be achieved for pollutants in the moving tidal
current travelling for such a long distance. It is anticipated that the
potential impacts to the nearby oyster beds would be insignificant.
Table 6.7
Comparison of the Leaching Trial Results with the New Zealand Guidelines for
Fresh and Marine Water Quality
Parameter
|
Leaching Trial Results
(mg/l)
|
New Zealand Water Quality Guidelines for the Inorganic
Chemicals (mg/l)
|
Required Dilution to Meet the Guidelines
|
Aluminium
|
900
|
<
10
|
>
90
|
Chromium
|
300
|
< 20
|
> 15
|
Cadmium
|
4
|
< 5
|
-
|
Copper
|
<75
|
< 5
|
> 15
|
Zinc
|
30
|
< 100
|
-
|
Nickel
|
<25
|
< 100
|
-
|
Iron
|
20
|
< 10
|
> 2
|
Lead
|
6
|
< 20
|
-
|
Manganese
|
3
|
< 100
|
-
|
Selenium
|
14
|
< 10
|
> 2
|
Arsenic
|
3
|
< 30
|
-
|
Source:
Australian and New Zealand Guidelines to Fresh and Marine Water Quality –
Volume 1 (July 1999)
Table 6.8
Comparison of the Leaching Trial Results with the UK Water Quality Standards
for the Protection of Saltwater Life
Parameter
|
Leaching
Trial Results (mg/l)
|
UK
Water Quality Standards (mg/l)
|
Required
Dilution to Meet the Standards
|
Aluminium
|
900
|
-
|
-
|
Chromium
|
300
|
15
|
>20
|
Cadmium
|
4
|
2.5
|
>1.6
|
Copper
|
<75
|
5
|
>15
|
Zinc
|
30
|
40
|
-
|
Nickel
|
<25
|
30
|
-
|
Iron
|
20
|
1000
|
-
|
Lead
|
6
|
25
|
-
|
Manganese
|
3
|
-
|
-
|
Selenium
|
14
|
-
|
-
|
Arsenic
|
3
|
25
|
-
|
6.6.1.22
Table 6.9 lists the chemical toxicity data for aquatic
life. LC50 (concentration at which 50% mortality occurs) of
the heavy metals for the species that could be found in Deep Bay are
present. Based on the available data of the LC50, exposure of polychaete worm to aluminium of 405 mg/L for 96 hours would cause 50%
mortality. The maximum concentration of aluminium (900 mg/L) detected in the leaching trials
is higher than the reference concentration. A dilution rate of 3 times of
the initial concentration would reduce the maximum concentration of aluminium
to around 300mg/L. It
is also observed that exposure of mytilus edulis to zinc of 30 mg/L for 14 days would cause 50% mortality.
A dilution rate of 3 times of the initial concentration of zinc (30 mg/L) is required to reduce the
maximum concentration to around 10 mg/L. This low dilution rate is likely to be achieved in a moving
water environment. The potential impact due to high concentration of
aluminium would be insignificant. The concentrations of other parameters
from the leaching trials are much lower than the corresponding LC50
concentrations.
6.6.1.23
As the leakage through
the base of the East Lagoon would not be significant, the PFA leachate in the East Lagoon is unlikely to cause
unacceptable impact on the aquatic environment from an ecotoxicological
point of view. The site conditions of East Lagoon during construction and
operational phases would not be much different from the existing
conditions. As the ash would remain in the East Lagoon and would not be
disposed of, detailed ecotoxicological assessment and
additional toxicity test are considered not necessary.
Table 6.9
Chemical Toxicity Data for Aquatic Life
Parameter
|
Leaching Trial Results
(mg/l)
|
Crassostrea gigas
(Pacific Oyster)
|
Mytilus edulis
(Common Bay Mussels)
|
Oryzias laptipes
(Medala, high-eyes)
|
Scylla serrata
(Green Crab)
|
Crangon crangon
(Common Shrimps)
|
Artermia salina
(Brine Shrimps)
|
Amphiphods
|
Polychaete Worm
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
LC50
|
Conc.
(mg/L)
|
Aluminium
|
900
|
48h
|
1000000
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
3d
|
3100
|
-
|
-
|
96h
|
405
|
Chromium
|
300
|
-
|
-
|
-
|
-
|
96h
|
120000
|
-
|
-
|
48h
|
100000
|
24h
48h
|
5300
3540
|
-
|
-
|
96h
|
1000
|
Cadmium
|
4
|
4h
96h
|
85
19500
|
96h
|
960
|
48h
|
560000
|
-
|
-
|
96h
|
460
|
24h
48h
|
3100
1540
|
4d
|
14.5
|
10d
28d
|
83
39
|
Copper
|
<75
|
14h
96h
|
100
560
|
10d
|
45
|
24h
48h
|
610
410
|
-
|
-
|
48h
|
10000
|
24h
48h
|
800
440
|
-
|
-
|
4d
28d
|
77
44
|
Zinc
|
30
|
4d
|
100
|
14d
|
10
|
24h
|
20000
|
-
|
-
|
48h
|
100000
|
24h
48h
|
4460
1700
|
-
|
-
|
28d
|
350
|
Nickel
|
<25
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
48h
|
100000
|
48h
|
162985
|
-
|
-
|
7d
10d
|
7700
16090
|
Iron
|
20
|
-
|
-
|
-
|
-
|
24h
|
18500
|
-
|
-
|
48h
|
33000
|
-
|
-
|
-
|
-
|
-
|
-
|
Lead
|
6
|
-
|
-
|
105h
150h
|
5000
500
|
24h
48h
|
350000
205000
|
-
|
-
|
96h
|
63000
|
24h
48h
|
10000
5010
|
-
|
-
|
96h
28d
|
7660
1430
|
Manganese
|
3
|
-
|
-
|
-
|
-
|
24h
|
1000000
|
-
|
-
|
48h
|
3300
|
-
|
-
|
-
|
-
|
-
|
-
|
Selenium
|
14
|
-
|
-
|
-
|
-
|
-
|
-
|
24h
72h
|
68000
33000
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
-
|
Arsenic
|
3
|
21d
|
10
|
-
|
-
|
-
|
-
|
-
|
-
|
96h
192h
|
96000
70000
|
24h
|
1.3
umol/L
|
-
|
-
|
96h
|
7400
|
Note:
The media type of the underlined data is freshwater
and the media type is marine water for the other data.
Source of information: Ecotox
Database System
6.6.2
Operation Phase
6.6.2.1
Potential sources of
water quality impact associated with the operation of the proposed STF have
been identified and include:
l
Wastewater generated from the operation of the STF;
l
Discharge of saline water from the proposed desalination
plant; and
l
Possible emission of microbes associated with the
transportation, storage and handling of dewatered sewage sludge.
Wastewater from the STF Operation
6.6.2.2
During the operation of
the STF, wastewater would be generated from sanitary facilities used by plant
personnel, commercial activities and sludge treatment activities in the STF
plant. The commercial activities in the STF mainly include the restaurant
trade as there would be a canteen in the future development of STF. In
addition, the source of wastewater from sludge treatment activities is mainly washdown water including plant washdown,
flushing, and vehicle washing etc. Cooling water used for cooling the
incinerator flue gas before entrance to the baghouse
filter would be completely recycled within the incineration system. Water
used in the boiler in heat recovery system would be completely
recycled within the incineration system or vaporized. Thus there
would not be any discharge of water from the facility.
6.6.2.3
There would be 60
employees working at the STF and the average flow of domestic wastewater
generated would be approximately 13.8 m3 per day. Moreover,
the washdown water generated from the sludge
treatment activities is estimated to be approximately 11.0 m3 per
day. Therefore, the total average sewage flow generated during the
operation of the STF would be approximately 24.8 m3 per day.
6.6.2.4
According to the above estimation,
an on-site wastewater treatment plant will be provided with a maximum capacity
of 100 m3 per day. All wastewater generated at the facility
will be discharged to the on-site wastewater treatment plant and treated by the
process of Membrane Bioreactor (MBR). In case of emergency situation in
which sewage needs to by-pass the treatment system, the sewage will be conveyed
to a sewage holding tank with a storage capacity of 2-day average flow.
6.6.2.5
The treated effluent
from the wastewater treatment plant would be reused for plant washdown, uncontrolled landscape irrigation, vehicular
washing, toilet flushing and groundskeeping in the
STF development, and there would be no wastewater effluent discharged to the
coastal waters of Deep Bay. Table 6.10 shows the summary of
wastewater generated and reused in STF.
6.6.2.6
The water quality
standards for the reclaimed water are set out based on other local effluent
reuse schemes. In Hong Kong, effluent reuse has been tried out in the Ngong Ping STW in Lantau Island
and the Shek Wu Hui STW in
North District.
Table 6.10
Summary of Wastewater Generated and Reused in STF
|
Quantity (m3/d)
|
Wastewater Generated from STF
|
Employees
activities
|
13.8
|
Sludge
treatment activities
|
11.0
|
Total
|
24.8
|
Reclaimed Water Demand from STF
|
Landscape
Irrigation Note 1
|
144.0
|
Plant washdown
|
11.0
|
Toilet
flushing, vehicle washing and groundskeeping
|
4.3
|
Total
|
159.3
|
Note:
1.
The amount is estimated based on the approximate total landscape area of 12,000
m2 and an assumption of evaporation rate of 12L/d/m2.
6.6.2.7
The water quality
standards set for the reuse of the Ngong Ping treated
effluent (the Limiting Standards) were agreed in 2002. The intended key
usages were toilet flushing and controlled irrigation. The parameters
were then set taking into account of the tertiary treatment standard prescribed
for the Ngong Ping STW, the standards adopted
previously for salt water supply for flushing purpose in Hong Kong, as well as
making reference to other overseas’ relevant standards. This set of
Limiting Standard was hence adopted for the design and construction of Ngong Ping STW. As part of the 2002 study, it was
further agreed that, in case if human contact with the treated effluent is
expected (e.g. unrestricted irrigation), then it would be necessary for the
turbidity to be tightened from 10 to 5 NTU, and also for the E. coli standard
to be tightened from 100 cfu/100 ml to non-detectable level.
6.6.2.8
Apart from the Ngong Ping project, an additional trial was undertaken by
EPD in 2004 as the Shek Wu Hui
STW Demonstration Scheme which generated treated effluent for non-potable uses
including toilet flushing, unrestricted irrigation, as well as ornamental water
features such as fish pond. As compared to the Ngong
Ping scheme, the Shek Wu Hui
STW Demonstration Scheme adopted a somewhat similar but more stringent set of
criteria (the Adopted Criteria) making reference to the generic USEPA reuse
standards as well as the “Title-22: California Water Recycling Criteria”
established by the California Department of Health Services. These
standards are designed to provide the highest possible degree of treatment
under varying circumstances. For example, the turbidity requirement is as
low as 2 NTU and the fecal coliform
bacterial level is required to be non-detectable.
6.6.2.9
Table 6.11 summarizes the effluent reuse standards for
the Ngong Ping project, the Shek
Wu Hui STW Demonstration Scheme, USEPA and the
proposed standards for this project. This project adopts the effluent
reuse standards for the Shek Wu Hui
STW Demonstration Scheme.
Table 6.11
Summary of Effluent Reuse Standards for Local Effluent Reuse Schemes, USEPA and
This Project
Parameter
|
Local
Effluent
Reuse
Scheme
|
USEPA
|
This
Project
|
Ngong Ping
|
SWHSTW
|
pH
|
-
|
6-8
|
6 – 9
|
6-8
|
BOD (mg/L)
|
< 10
|
< 10
|
< 10
|
< 10
|
Turbidity (NTU)
|
< 10 Note1
|
< 2
|
< 2
|
< 2
|
TSS (mg/L)
|
< 10
|
-
|
-
|
-
|
Total Coliform/ 100ml
|
<100 Note1
|
Non detectable
|
Non detectable
|
Non detectable
|
Chlorine Residual (mg/L)
|
> 0.5
|
> 1
|
> 1
|
> 1
|
Note:
1.
Turbidity and E-coli level were
suggested to be lowered to <5 NTU and non detectable respectively in case if
use for unrestricted irrigation were required i.e. human contact with the treated
effluent and/or aerosol is likely.
Discharge of Saline Water from
Desalination Plant
6.6.2.10
Approximately 1,000 m3/day
of saline water would be discharged from the proposed desalination plant for
domestic consumption, process water requirement and plant washdown,
flushing, vehicle washing, groundskeeping and
landscape irrigation for STF daily operation. The characteristics of the
saline water discharge are summarized below:
l
pH will be raised from feed of 8.0 - 8.5 to reject of
8.2 - 8.8;
l
Salinity will be raised from feed of 30,000 - 35,000
mg/L to reject of 50,000 - 58,333 mg/L;
l
Suspended solids (SS) will be raised 1.7 times of feedwater (seawater); and
l
Biochemical oxygen demand (BOD) will be concentrated
1.7 times of feedwater (seawater).
6.6.2.11
Given that the
discharge would comprise concentrated saline water only, at a concentration of
about 1.7 times of the feedwater (seawater), with a
low discharge volume, adverse impacts on water quality would not be
expected. A comparison of the characteristics of the saline water
discharge with the standards for effluents discharged into the coastal waters
of Deep Bay Water Control Zone is given in Table
6.12 below.
Table 6.12 Comparison of
Saline Water Discharge from Desalination Plant with Effluent Discharge Standard
Parameter
|
Saline Water Note 1
|
Discharge Standard Note
2 & 3
|
Compliance with Discharge
Standard
|
pH
|
< 8.8
|
6 – 9
|
Yes
|
Temperature (oC)
|
25 – 35
|
45
|
Yes
|
Suspended solids (mg/L)
|
20.1
|
25
|
Yes
|
BOD 5-day (mg/L)
|
1.9
|
10
|
Yes
|
Note:
1.
Feedwater assumed to have a pH of 8.1, SS of 11.8 mg/L
and BOD of 1.1 mg/L, as based on water quality monitoring results of EPD
monitoring station DM4 for the year 2004
2. Discharge standard for flow rate of
>1000 and 1500 m3/day
3. The effluent discharge standards do not specify
a standard for salinity
Possible Emission of Microbes
Associated with Transportation, Storage and Handling of Dewatered Sewage Sludge
6.6.2.12
The possible emission
of microbes associated with the transportation, storage and handling of
dewatered sewage sludge into surrounding waterbodies
has been addressed in Section 4 under the health risk assessment associated
with the STF operation. The following features have been incorporated
into the design of the STF to prevent microbes entering the surrounding water
bodies during the transportation, storage and handling process:
l
Dewatered sludge would be transported in water-tight
ISO-type shipping containers from the SCISTW and SHWSTW by marine vessel to the
WENT Landfill pier;
l
Dewatered sludge from the other regional STW would be
transported by road in water-tight containers or skips, or in truck mounted
container trucks, to the STF; and
l
A drainage system would be provided at the receiving
area of the STF to collect drainage water during cleaning of the floor
area. The drainage water would be routed to the on-site wastewater
treatment plant.
6.6.2.13
As discussed in Section
4.3, the following “risk control measures” identified as existing/expected
safeguards during the operation of the STF are also applicable as water
pollution prevention measures:
l
Detection device/alarm should be installed to prevent
overfilling of temporary sludge storage tank;
l
Frequent and sufficient maintenance should be provided
for the drainage system of STF; and
l
Multiple outlets in drainage system should be designed
and provided to reduce the likelihood of drainage blockage.
6.7
Mitigation Measures
6.7.1
Introduction
6.7.1.1
Proposed mitigation
measures for containing and minimizing water quality impacts are summarised
below.
6.7.2
Construction Phase
Construction Site Run-off and
Drainage
6.7.2.1
The site practices outlined in ProPECC PN 1/94 “Construction Site Drainage” should be
followed as far as practicable in order to minimise surface runoff and the
chance of erosion. These practices include the following items:-
l
At the start of site establishment, internal drainage
works and erosion and sedimentation control facilities should be implemented.
Channels, earth bunds or sand bag barriers should be provided on site to
direct stormwater to silt removal facilities.
The detailed design and installation of the temporary on-site drainage system
should be undertaken by the contractor prior to the commencement of
construction;
l
Before commencing any site formation work, all sewer
and drainage connections should be sealed to prevent debris, soil, sand etc.
from entering public sewers/drains;
l
Boundaries of earthworks should be surrounded by dykes
or embankments for flood protection, as necessary;
l
Sand/silt removal facilities such as sand traps, silt
traps and sediment basins should be provided to remove sand/silt particles from
runoff to meet the standards of the Technical Memorandum under the Water
Pollution Control Ordinance. The design of silt removal facilities should
be based on the guidelines provided in ProPECC PN
1/94. All drainage facilities and erosion and sediment control structures
should be inspected monthly and maintained to ensure proper and efficient
operation at all times and particularly during rainstorms;
l
Water pumped out from foundation piles must be
discharged into silt removal facilities;
l
During rainstorms, exposed slope/soil surfaces should
be covered by a tarpaulin or other means, as far as practicable. Other
measures that need to be implemented before, during and after rainstorms are
summarized in ProPECC PN 1/94;
l
Exposed soil areas should be minimized to reduce
potential for increased siltation and contamination of runoff;
l
Earthwork final surfaces should be well compacted and
subsequent permanent work or surface protection should be immediately
performed;
l
Open stockpiles of construction materials or
construction wastes on-site should be covered with tarpaulin or similar fabric
during rainstorms; and
l
All vehicles should be cleaned before leaving the works
area to ensure no earth, mud and debris is deposited on roads. An
adequately designed and sited wheel washing bay should be provided at every
site exit. The wheel washing facility should be designed to minimize the
intake of surface water (rainwater). Wash-water should have sand and silt
settled out and removed at least on a weekly basis to ensure the continued
efficiency of the process.
General Construction Activities
6.7.2.2
Debris and refuse generated on-site should be
collected, handled and disposed of properly to avoid entering the nearby water
bodies and public drainage system. Stockpiles of cement and other
construction materials should be kept covered when not being used.
6.7.2.3
Oils and fuels should only be used and stored
in designated areas which have pollution prevention facilities. To
prevent spillage of fuels and solvents to nearby water bodies and public
drains, all fuel tanks and storage areas should be provided with locks and be
sited on sealed areas, within bunds of a capacity equal to 110% of the storage
capacity of the largest tank. The bund should be drained of rainwater
after a rain event.
Sewage from Construction Workforce
6.7.2.4
Temporary sanitary facilities, such as portable
chemical toilets, should be employed on-site where necessary to handle sewage
from the workforce. A licensed contractor would be responsible for
appropriate disposal and maintenance of these facilities.
Release of PFA Leachate from Ash Lagoon into
the Aquatic Environment
6.7.2.5
The past
monitoring data showed that the water quality at the location outside the ash
lagoon area was not affected by the PFA filling operation. Although the liner installed at the base of
the lagoons would have been creaked / broken, the low
permeability values of the marine deposits and alluvium underneath the PFA
layer would limit the seepage of PFA leachate.
The foundation construction of the STF is not likely to accelerate the release
of PFA leachate through the base of the lagoon site.
6.7.2.6
Environmental
monitoring and audit (EM&A) should be included to ensure that the
foundation construction would not cause unacceptable release of PFA leachate into the Deep Bay waters. The parameters to
be measured should include the heavy metals such as cadmium, chromium and
aluminium, which have the greatest tendency to leach from the lagooned PFA into the seawater. Details of the
measurement requirements are presented in the EM&A manual
6.7.3
Operation Phase
Receiving Area in the STF
6.7.3.1
An adequate number of
drains should be provided at the receiving area of the STF with drain piping for
draining and cleaning all areas of the floor. The floors should be
adequately sloped to floor drains for collection of drainage water during
cleaning. Such floor drains should contain no traps. The drainage
water should be routed to an outdoor vented and trapped manhole for connection
to the on-site wastewater treatment plant.
Wash Down Facilities at STF
6.7.3.2
Frequent and sufficient
maintenance should be provided for the drainage system, and multiple outlets in
the drainage system should be designed and provided to reduce the likelihood of
drainage blockage.
Temporary Sludge Storage at STF
6.7.3.3
A detection
device/alarm should be installed to prevent overfilling of temporary sludge
storage tank.
6.8
Residual Environmental
Impacts
6.8.1.1
With the full
implementation of the recommended mitigation measures for the construction and
operation phases of the proposed Project, no unacceptable residual impacts on
water quality are expected. It is recommended that regular audit of the
implementation of the recommended mitigation measures at the work areas be
carried out during the construction phase. No wastewater effluent will be
discharged into the Deep Bay WCZ during the operation of the STF and hence no
residual water quality impact is envisaged.
6.9
Environmental Monitoring and Audit
6.9.1.1
To ensure no adverse
water quality impact to the nearby stream due to the discharge of surface
runoff and drainage from the works areas, water quality monitoring of the Tsang
Kok stream is recommended during site formation and
the widening of the access road. Marine water quality monitoring is also
recommended during foundation pilling of the STF to ensure that the foundation
construction would not cause an unacceptable release of PFA leachate
into the Deep Bay waters. Details of the recommended water quality
monitoring parameters to be measured and monitoring locations are provided in
the stand-alone EM&A Manual for the Project. It is also recommended
that regular site inspections be undertaken to inspect the construction
activities and works areas in order to ensure the recommended mitigation measures
are properly implemented.
6.9.1.2
Monitoring of the
discharge quality of effluent from land-based construction sites should be
conducted by the Contractor. A detailed effluent sampling programme for
water quality control during the construction phase should be submitted to EPD
for approval prior to commencement of the construction works.
6.9.1.3
Monitoring of water
quality would not be required during the operation phase of the STF as there
would be no wastewater effluent discharge from the on-site wastewater treatment
plant.
6.10
Conclusion
6.10.1.1
The potential sources
of water quality impact arising during the construction phase of the Project
include construction site runoff and drainage, wastewater generated from
general construction activities and sewerage from the workforce. With
implementation of the recommended mitigation measures and site practices
outlined in ProPECC PN 1/94, no unacceptable residual
impacts on water quality are expected.
6.10.1.2
During the operation
phase of the Project, wastewater will be generated from sanitary facilities
used by plant personnel, commercial activities and sludge treatment activities
in the STF. An on-site wastewater treatment plant will be provided.
All generated wastewater will be discharged to the on-site wastewater treatment
plant and treated by the process of MBR. The treated effluent from the
wastewater treatment plant will be reused in the STF and there would be no
wastewater effluent discharged to the coastal waters of Deep Bay.
6.10.1.3
Saline water would be
discharged from the proposed desalination plant in a low discharge rate.
The saline water discharged from the desalination plant will comply with the
standards for effluents discharging into the coastal waters of Deep Bay Water
Control Zone. Adverse impacts on water quality would not be
expected.
6.10.1.4
To prevent potential
emission of microbes during transportation, storage and handling of dewatered
sewage sludge into surrounding waterbodies, proper
design of the STF will be conducted and the recommended “risk control measures”
will be implemented. No unacceptable water quality impacts are expected.