1                                            Introduction

This Method Statement presents information on the approach for the water quality assessment and modelling works for the study.  The methodology has been based on the following three focus areas, as follows:

·       Model Selection;

·       Input Data; and,

·       Scenarios.

1.1                                      Interpretation of the Requirements: Key Issues and Constraints

The objectives of the modelling exercise are to assess:

·       Effects of construction, which comprises the study of the dispersion of sediments released during construction, including the installation of a submarine pipeline, water main and power cables;

·       Effects of operation due to reclamations (affecting flows and potentially water quality due to changing flows); discharges (potentially affecting temperatures and water quality due to chlorine or other antifoulants); and maintenance dredging (potentially increasing suspended solids in water column);

·       Any residual impacts, which include any change in hydrodynamic regime; and,

·       Any cumulative impacts due to other projects or activities within the study area.

The construction and operational effects have been studied by means of mathematical modelling using existing models that have been set up by WL | Delft Hydraulics (Delft) on behalf of the Environmental Protection Department (EPD) or approved by the EPD for use in environmental assessments. 

1.2                                      Model Selection

The existing Western Harbour Model of the Delft 3D water quality (WAQ) and hydrodynamic suite of models have been used to simulate effects on hydrodynamics and water quality.  These models have been calibrated as part of the Landfill Extension Study.

The WAQ model has been used to simulate water quality impacts during construction and operation of the facility.  The existing Update model has the required spatial extent.  The existing grid of the model in the vicinity of South Soko and Black Point are shown in Figure A1.1 and Figure A1.2.

Figure A1.1    Model Grid of the Update Model in the Vicinity of Soko Islands

Text Box: 2 km

 

                            

Figure A1.2    Model Grid of the Update Model in the Vicinity of Black Point

Text Box: 4 km

 

                       

As seen in Figures A1.1 and A1.2, the grid size of the existing model near the site is in the order of about 300 m.  It was, therefore, considered appropriate to carry out refinement of the water quality and hydrodynamic grids to provide improved resolution (less than 75 m) in key areas of interest.  The refinements of the model grid of the Update Model in the vicinity of Soko Islands and Black Point are shown in Figure A1.3 and Figure A1.4 respectively.

 


Figure A1.3    Refinement of Model Grid of the Update Model in the Vicinity of Soko Islands

                  


Figure A1.4    Refinement of Model Grid of the Update Model in the Vicinity of Black Point

                  

 


1.3                                      Coastline & Bathymetry

Hydrodynamic data have been obtained using coastline and bathymetry for a time horizon representative of the construction and operation of the facility (i.e., 2007 onwards).  Figures A1.5a, A1.5b and A1.6 show the bathymetry and coastline during construction phase, whereas Figure A1.7 during operational phase at the LNG terminal at South Soko Island.

Figure A1.5a  Bathymetry and Coastline in the Vicinity of Black Point (2007 onwards)

 


Figure A1.5b  Coastline Used in the Model for the Project Area (2007 onwards)

                    

Figure A1.6    Bathymetry and Coastline in the Vicinity of South Soko Island (2007 onwards)

                      

Figure A1.7    Operational Bathymetry at South Soko

             

1.4                                      Vector Information

The current patterns in the project area are presented in Figures SK_B01-B08 (pre-project situation) and Figures SK_F01-08 (post-project situation). 

Under pre-project situation, the plots indicate that, in general, for the area in around the LNG terminal in South Soko Island current velocities rarely exceed 0.2 m s-1 in the dry season and 0.3 m s-1 in the wet season.  Maximum current velocities appear to be in the order of 0.6 m s-1 in the dry season and 2 m s-1 in the wet season, in areas predominantly offshore, or on the south western headland of South Soko Island. 

Under post-project situation, the current velocities are likely of similar magnitude at both seasons.

1.5                                      Information on Model Inputs

Details on the model input parameters are presented in Appendix A in this Annex.

1.6                                      Uncertainties in Assessment Methodologies

Uncertainties in the assessment of the impacts from suspended sediment plumes should be considered when drawing conclusions from the assessment.  In carrying out the assessment, the worst case assumptions have been made in order to provide a conservative assessment of environmental impacts.  These assumptions are as follows:

·       The assessment is based on the peak dredging and filling rates.  In reality, these will only occur for short period of time; and,

·       The calculations of loss rates of sediment to suspension are based on conservative estimates for the types of plant and methods of working.

The conservative assumptions presented above allow a prudent approach to be applied to the water quality assessment.

The following uncertainties have not been included in the modelling assessment.

·       Ad hoc navigation of marine traffic;

·       Near shore scouring of bottom sediment; and

·       Access of marine barges back and forth the site.

 

 


2                                            Water QUALITY Sensitive Receivers

The water quality sensitive receivers (SRs) have been identified in the EIA (Part 2 - Section 6: Water Quality Assessment) in accordance with Annex 14 of the Technical Memorandum on EIA Process (EIAO, Cap.499, S.16). These SRs are illustrated in Figure A2.1 and listed in Table A2.1. In addition to the SRs, there are other additional water modelling output points at some representative locations are selected for further analysis (thereinafter regarded as MPs) and they are shown in Table A2.2 and also presented in Figure A2.1.  EPD routine water quality monitoring stations are shown in Table A2.3 for reference.  

Table A2.1      Water Quality Sensitive Receivers (SRs) around Proposed LNG Terminal at South Soko and Black Point and the Submarine Pipeline Section from South Soko to Black Point

Sensitive Receiver

Name

Water Quality Modelling Output Location

Included in the Model

Fisheries Resources

 

 

 

Spawning/
Nursery Grounds

Fisheries Spawning/
Nursery Grounds in South Lantau

SR16b, SR24, SR27

Yes

Fisheries Spawning Ground in North Lantau

SR8

Yes

Artificial Reef Deployment Area

Sha Chau and Lung Kwu Chau

SR6e

Yes

Northeast Airport

SR7d

Yes

Fish Fry Habitat

Pak Tso Wan

SR16b

Yes

Fish Culture Zone

Cheung Sha Wan

SR38

No

 

Ma Wan

SR40a-b

No

Marine Ecological Resources

 

 

Seagrass Beds

Pak Nai

SR2

Yes

Marine Park

Designated Sha Chau and Lung Kwu Chau

SR6a-d

Yes

Potential Marine Park

South West Lantau

SR19a-c

Yes

Mangroves

Pak Nai

SR2

Yes

Intertidal Mudflats

Pak Nai

SR1

Yes

Tai O

SR12

Yes

Yi O

SR14

Yes

Shui Hau Wan

SR33

Yes

Horseshoe Crab Nursery Grounds

Pak Nai

SR1

Yes

Sham Wat Wan

SR10

Yes

Tai O

SR12

Yes

Yi O

SR14

Yes

Sha Lo Wan

SR18

Yes

Tong Fuk Miu Wan

SR33

 

Tung Chung Bay

SR39

Yes

Protection Zone

Chinese White Dolphin Protection Zone in Mainland Waters

 

SR11, SR11a-b

Yes

Water Quality Sensitive Receivers

 

 

Gazetted Beaches

Butterfly Beach

SR5c

Yes

Tuen Mun Beaches

SR5d

No

Tong Fuk

SR34

Yes

Upper Cheung Sha Beach

SR35

Yes

 

Lower Cheung Sha Beach

SR36

No

 

Pui O Wan

SR37

No

Non-gazetted Beaches

Lung Kwu Sheung Tan

SR5a

Yes

 

Lung Kwu Tan

SR5b

Yes

 

Fan Lau Sai Wan

SR15a

Yes

 

Fan Lau Tung Wan

SR15b

Yes

 

Tsin Yue Wan

SR15c

Yes

Seawater Intakes

Black Point Power Station

SR4

Yes

Castle Peak Power Station

SR7a

Yes

Tuen Mun Area 38

SR7b

Yes

Airport

SR7c-f

Yes

 

Tuen Mun WSD

SR7h

No

Table A2.2      Water Quality Modelling Output Points (MPs) around Proposed LNG Terminal at South Soko and Black Point and the Submarine Pipeline Section from South Soko to Black Point

Sensitive Receiver

Name

Water Quality Modelling Output Points

Included in the Model

Representative Intertidal & Subtidal Coastal Location

Kau Ling Chung (Rocky)

MP23, MP25-26, MP28-30

Yes

Tai Long Wan (Sandy)

MP20-21

Yes

Kau Ling Chung

MP23

Yes

Operational Seawater Intake

South Soko Island

MP40

Yes

 


Table A2.3      EPD Routine Water Quality Monitoring Stations in the Vicinity of the Project Area

EPD Monitoring Stations

Respective WCZ

Included in the Model

DM4, DM5

Deep Bay WCZ

No

NM5, NM6, NM8

North Western WCZ

No

SM13, SM17, SM20

Southern WCZ

No

 

 


3                                            Construction Phase

For the construction phase the WAQ model has been used to directly simulate the following parameters:

·       suspended sediments; and

·       sediment deposition.

It is assumed that the worst-case construction phase impacts will be at the commencement of dredging, when there is no depression formed to trap sediments disturbed during works. 

Note that DO, TIN and NH3-N are calculated using the modelled maximum SS concentrations as shown in Section 6: Water Quality Impact Assessment.

3.1                                      Working Time

South Soko Island is relatively remote in nature and for water quality modelling a 24 working hours per day and 7 working days per week is assumed.  Exception is given to submarine water mains construction and cable circuit installation.  The former assumed 16 working hours per day at all locations except at the land and launching point where 24 working hours per day were assumed, and 7 working days per week while the latter assumed 12 working hours per day and 6 working days per week.  These time differences relate to typical practices by contractors in Hong Kong that would be involved in these works.  Working hours for gas receiving station at Black Point are assumed to be 16 per day and 7 working days per week.

The assumption of working time in the model is summaries in Table A3.1.

Table A3.1      A Summary of Working Time Assumed in the Model for Various Construction Activities

Construction Activities

Locations

Assumption of Working Time

Seawall Construction

Eastern berth at South Soko Island

24 hours per day and 7 days per week

 

 

Western berth at South Soko Island

24 hours per day and 7 days per week

 

Approach Channel and Turning Basin

South of South Soko Island

24 hours per day and 7 days per week

 

Submarine Water Main

Landing point (using the common shore approach with cable)

 

24 hours per day and 7 days per week

 

 

Other section in the open waters

16 hours per day and 7 days per week

Submarine Cable Circuit

Landing point (using the common shore approach with cable)

 

24 hours per day and 7 days per week

 

Other section in the open waters

 

12 hours per day and 6 days per week

Submarine Gas Pipeline

From South Soko Island to Black Point

 

For grab dredging, 12 hours per day (daytime) and 7 days per week

For THSD dredging, 24 hours per day and 7 days per week

Submarine Gas Pipeline (Gas Receiving Station)

Black Point

16 hours per day and 7 days per week

3.2                                      Overview of Dredging Plants

3.2.1                                Grab Dredgers

Grab dredgers will be utilised in the dredging works for the reclamation works at the terminal as well as the navigation channel, turning circle and berthing box.  Also the submarine water mains, some sections of the submarine pipeline and the gas receiving station may need to be pre-trenched and this is likely to be done utilising a grab dredger.

Grab dredgers may release sediment into suspension by the following mechanisms:

·       Impact of the grab on the seabed as it is lowered;

·       Washing of sediment off the outside of the grab as it is raised through the water column and when it is lowered again after being emptied;

·       Leakage of water from the grab as it is hauled above the water surface;

·       Spillage of sediment from over-full grabs;

·       Loss from grabs which cannot be fully closed due to the presence of debris;

·       Release by splashing when loading barges by careless, inaccurate methods; and

·       Disturbance of the seabed as the closed grab is removed.

In the transport of dredging materials, sediment may be lost through leakage from barges.  However, dredging permits in Hong Kong include requirements that barges used for the transport of dredging materials have bottom-doors that are properly maintained and have tight-fitting seals in order to prevent leakage.  Given this requirement, sediment release during transport is not proposed for modelling and its impact on water quality is not addressed under this Study.

Sediment is also lost to the water column when discharging material at disposal sites.  The amount that is lost depends on a large number of factors including material characteristics, the speed and manner in which it is discharged from the vessel, and the characteristics of the disposal sites.  As impacts due to disposal operations at potential disposal sites have been assessed under separate studies, they are not addressed further in this document. 

Loss rates have been taken from previously accepted EIAs in Hong Kong ([1]) ([2]) and has been based on a review of world wide data on loss rates from dredging operations undertaken as part of assessing the impacts of dredging areas of Kellett Bank for mooring buoys ([3]). The assessment concluded that for 8 m3 (minimum) grab dredgers working in areas with significant amounts of debris on the seabed (such as in the vicinity of existing mooring buoys) that the loss rates would be 25 kg m-3 dredged, while the loss rate in areas where debris is less likely to hinder operations would be 17 kg m-3 dredged. 

For this Study it is proposed that the loss rate of 17 kg m-3 dredged for grab dredging (grab size of 12/16 m3) be used as geophysical surveys have shown that there are no significant quantities of debris in the vicinity of the dredging works ([4]). 

Generally, a split-bottom barge could have a capacity of 900 m³. A bulk factor of 1.3 would normally be applied, giving a dredging rate of 700 m³ per barge. The hopper dry density for an 800 to 1,000 m3 capacity barge is around 0.75 to 1.24 ton m-3. 

The average release rates will, in fact, be somewhat less than those indicated above. The instantaneous dredging (and loss) rates will also decrease as the depth increases. This is because the assumed dredging production rates are instantaneous rates that will not be maintained due to delays for breakdowns, maintenance, crew changes and time spent relocating the dredgers. The release rates that are to be modelled area, therefore, considered to represent conservative conditions that will not prevail for any great length of time. 

A review of the vector plots at the sites allowed identification of areas that would disperse sediment further than other areas due to higher current velocities.  These areas were consequently chosen as the locations of the sources of sediment in the model. 

3.2.2                                Trailing Suction Hopper Dredgers

Trailing Suction Hopper Dredgers (TSHD) will be used mainly for the approach channel and turning circle. It may also be deployed during the dredging for the submarine gas pipeline. 

The hopper dry density for a TSHD is typically 0.75 ton m-3. TSHD could dredge at a faster rate than grab dredgers (typical dredging rate of 5,400 m3 per trip per TSHD with a maximum dredging rate up to 7,200 m3 per trip depending on the vessel size).  For the modelling scenarios it has been assumed that the Contractor will utilise a small (<5,000 m3) to medium (5,000 – 10,000 m3) TSHD. 

A review of international data on losses from trailer dredgers has determined that a loss rate of 7 kg m-3 dredged would be appropriate irrespective of the size of the dredger, assuming no overflowing but that the Lean Mixture Overboard (LMOB) systems are in operation ([5]) ([6]) ([7]). LMOB is used at the beginning and end of the dredging cycle when the suction arm is being lowered and raised.  At these times the majority of the material entering the hopper will be water with small amounts of fine sediments, which is discharged to the sea via the overflow system. 

Overflowing refers to the discharge of fine sediment and water during bulk dredging and results in high losses of sediment to suspension. Overflowing is not usually permitted when dredging in marine mud and is usually only allowed during dredging of sand deposits, when overflowing is utilised to increase the density of the material in the hopper. 

The value of 7 kg m-3 (1) (2) (3) dredged for dredging using trailing suction hopper dredgers will be appropriate for this Study as LMOB will be used but overflowing will not be permitted. It has also been assumed that no more than one THSD dredger will be operating at any one time. 

During dredging the drag head will sink below the level of the surrounding seabed and the seabed sediments will be extracted from the base of the trench formed by the passage of the draghead.  The main source of sediment release is the bulldozing effect of the draghead when it is immersed in the mud.  This mechanism means that sediment is lost to suspension very close to the level of the surrounding seabed and a height of 1 m has been adopted for the initial location of sediment release in the model.

Disposal site at South Cheung Chau is assumed to be available at the time of dredging works commissioned.  Contractor should confirm the availability of the disposal site prior to any disposal events.  Based on this assumption, the cycle time for a TSHD is calculated as presented in Table A3.2.

Table A3.2      Cycle Time for a TSHD

 

Disposal Site

TSHD Works Site

Distance (km)

Sailing Speed (km hr-1)

Off-site (Travel) Time (hr)

On-site Dredging Time (hr)

On-site Idle Time (hr)

Total Cycle Time (hr)

Working hours per day (hr)

Number of Cycles per day

(a)

(b)

(c)

(d)

(e) = 2* (c)/(d)

(f)

(g) = 2 hr - (f)

(h) = (e) + (f) + (g)

(i)

(j) = (i)/(h)

South Cheung Chau

South Soko

11

28.34

0.78

0.75

1.25

2.78

24

9

South Cheung Chau

Fan Lau Crossing

17

28.34

1.20

0.75

1.25

3.20

24

8

South Cheung Chau

Lantau Channel

24

28.34

1.69

0.75

1.25

3.69

24

6

South Cheung Chau

West Lantau

30

28.34

2.12

0.75

1.25

4.12

24

6

3.3                                      Jetting

The speed of the machine will progress depending on the construction type.  Jetting speeds have been taken as 65 m hr-1 for water mains construction, 150 m hr-1 for cable circuit installation and 21 m hr-1 for gas pipeline installation.  These rates relate to typical practices by contractors in Hong Kong that would be involved in these works.

The maximum burial depth for each installation will be 5 m.  For water mains and gas pipeline, it is envisaged that it will require three passes of the jetting machine to reach the required burial depth.  The volumes of sediment disturbed will vary depending upon whether it is the first, second or third pass.  The consecutive passes may uplift the bottom sediment in a short period of time.  Despite, this will be temporary and instantaneous disturbance to the seabed since the disturbed sediment is expected to settle on the seabed in a short period after the jetting machine has passed.

For the water main, if we assume a conservative case for the third pass (17.5 m3 per m), the rate of disturbance will be 0.32 m3 s-1 (1).  Similarly, for the cable circuit installation, the rate of disturbance will be 0.06 m3 s-1 (1.5 m3 per m) (1).  The rate of disturbance for the pipeline will be 0.09 m3 s-1 (15 m3 per m) ([8]). 

The disturbed sediment will constitute a layer of fluid mud flowing across the seabed either side of the jetting machine and only a small portion of this sediment will enter the water column. 

It is conservatively assumed that 20% of the disturbed sediment enters suspension and this would give a loss rate.  The loss rate used here has been used in previous projects for submarine utility installations under the EIAO that have been installed using jetting methods and have obtained Environmental Permits:

·       The Proposed Submarine Gas Pipelines from Cheng Tou Jiao Liquefied Natural Gas Receiving Terminal, Shenzhen to Tai Po Gas Production Plant, Hong Kong – EIA Study (AEIAR-071/2003). EP granted on 23 April 2003 (EP-167/2003).

·       132kV Submarine Cable Installation for Wong Chuk Hang - Chung Hom Kok 132kV Circuits (AEP-126/2002).  EP granted on 2 April 2002 (EP-126/2002).

·       FLAG North Asian Loop (AEP-099/2001).  EP granted on 18 June 2001 (EP-099/2001).

·       East Asian Crossing (EAC) Cable System (TKO), Asia Global Crossing (AEP-081/2000).  EP granted on 4 October 2000 (EP-081/2000).

·       East Asian Crossing (EAC) Cable System, Asia Global Crossing (AEP-079/2000).  EP granted on 6 September 2000 (EP-079/2000).

·       Submarine Cable Landing Installation in Tong Fuk Lantau for Asia Pacific Cable Network 2 (APCN 2) Fibre Optic Submarine Cable System, EGS.   EP granted on 26 July 2000 (EP-069/2000).

·       Telecommunication Installation at Lot 591SA in DD 328, Tong Fuk, South Lantau Coast and the Associated Cable Landing Work in Tong Fuk, South Lantau for the North Asia Cable (NAC) Fibre Optic Submarine Cable System (AEP-064/2000).  EP granted in June 2000 (EP-064/2000).

 

To calculate the mass entrainment rate it is necessary to apply a dry density for the material, which is conservatively assumed to be 700 kg m-3.  The sediment will be entered into the model in the model layer closest to the seabed because this will represent the entrainment of sediment to suspension from the layer of fluid mud flowing over the existing seabed.  This approach is considered valid as the jetting machine is fluidising the seabed sediments and not excavating the sediments, consequently there will be little vertical entrainment of sediment into the water column.

The sediment will be entered into the model within a series of grid cells to represent the jetting machine moving along the pipeline route.  Thus each grid cell will represent a section of the pipeline route and sediment will be entered into that grid cell for the length of time it takes the jetting machine to pass the length of that cell, based on the jetting machine speeds given above.  Once the jetting machine has passed that grid cell, sediment will then be entered in the next grid cell on the route.  The sediment release in the bed layer (constitute 10 %) of the water column is assumed in the model.

It should be noted that the assumptions in the model has been adopted in the previous approved EIAs and a number of jetting contractors have confirmed that the assumptions adopted in the model for the jetting are reasonable and practical.  Further information of the jetting operation is presented in Annex 6K.

3.4                                      Dredging Scenarios

3.4.1                                Construction Works for Seawall and Reclamation Areas (Scenario 1)

Dredging

Dredging works will be carried out at eastern and western side of South Soko Island (Figure A3.1).  The estimated dredged volume under the seawalls and for the approach channel at western berth is approximately 0.28 Mm3 in total. 

With the assumption of 24 hours working at South Soko Island, the average dredging rate would become, 6,300 m3 (based on 12 m3 grab size) or 8,400 m3 day-1 (based on 16 m3 grab size).  At the site, taking a conservative assumption when the grabs are just commencing dredging in relatively shallow water and hence a higher production output, the maximum daily rate of production (with a minimum grab size of 8 m3) will be about 10,000 m3 day-1, giving a rate of release for the dredger of 1.97 kg s-1.    

Hence, two grab dredgers will be used for the continuous dredging with an emission of 1.97 kg s-1 (whole column).

In view that the inshore part of the eastern berth is too narrow that it does not cover a complete grid cell in the model.  A stationary emission point, SS01, is defined at the offshore breakwater.  Continuous release at SS01 is considered to be conservative and representative for the dredging area.  A stationary emission point, SS02, (Figure A3.1) is chosen at a location that has the shortest distance to the nearby sensitive receiver, i.e., fish fry habitat at Pak Tso Wan.  This will prevent any underestimation of the impacts to the habitat. 

Backfilling

Sandfilling for seawall trench and the reclamation at western berth by a pelican barge (rainbowing) is simulated by assuming a filling rate of 75,000 m3 day-1.  Working hours have been assumed to be 24 per day.  The fill material will be marine sand which generally has a fine content ranging from 2% to 10%.  As the source of material could not be confirmed at time of EIA compiled, the upper bound of the fine content, i.e. 10% is assumed for the conservative case.  The dry density of sand fill will be approximately 1,938 kg m-3.  A highly conservative loss rate of 10% is assumed, giving a rate of release of 16.8 kg s-1 (continuous in whole column).

Since the seawall trench and reclamation area is small and close to the shore which is covered by approximately two grid cells in the model, a stationary emission point, SS32, (Figure A3.1) has been chosen at a cell that well represents both the seawall trench and the reclamation.

3.4.2                                Construction Works for Water Main Installation (Scenarios 2 and 3)

The estimated dredged volume for the utility shore approach at South Soko and at Shek Pik is approximately 35,000 m3 and 37,000 m3, respectively.  At the existing marine sand borrow area and navigation channel, the estimated dredged volume is approximately 140,500 m3.  Working hours have been conservatively assumed to be 16 hours per day and 7 working days per week. 

The grab dredging will be operated at South Soko shore approach; Shek Pik shore approach; and waterway crossing sand borrow area and marine navigation channel and will be followed by backfilling operations.  Jetting will be used for post trenching near South Soko and Shek Pik. 

Grab Dredging (Scenario 2)

Grab dredging at three sections, i.e., South Soko Island shore approach, Shek Pik shore approach and waterway across sand borrow and marine channel, is modelled in Scenario 2.  Working hours have been conservatively assumed to be 16 per day.  Using the dredging rate of 8,000 m3 day-1 a continuous emission rate of 2.36 kg s-1 has been modelled throughout the whole water column. 

Figure A3.2 indicates the location of the water mains as well as the emission sources.  The dredging area at the shore is small and hence two stationary emission sources, SS09 and SS10, are chosen for the shore approaches at South Soko Island and Shek Pik respectively.  A moving source, SS08, is defined in the model to represent a longer section in the waterway.

Jetting (Scenario 3)

Following grab dredging there will be post trenching jetting at South Soko and Shek Pik sections.  Although the jetting works will be carried out one by one without overlapping, Scenario 3 simulates the most conservative case, i.e. the jetting works is conducted simultaneously at the two sections. 

Two moving sources (SS09 and SS10 in Figure A3.3) with continuous emission rates of 14.7 kg s-1, 29.5 kg s-1 and 44.2 kg s-1 are defined for the 1st, 2nd and 3rd passes respectively whereas the jetting rate to be 10,400 m3 day-1 and the dry density of sediment to be 700 kg m-3.  Working hours have been assumed to be 16 per day.  One of the moving sources (SS09) will start at west South Soko (extent seawards following the curve of the watermain over a distance of 1,700 m) and another (SS10) will begin at Shek Pik (extend seawards following the curve of the watermain over a distance of 2,300 m).  The speed of progress will be 65 m h-1 and three passes will be made without down time between passes.  As the disturbed layer would be confined to the seabed the emission will be put at bed layer (10% of the water column). 

3.4.3                                Construction Works for Approach Channel and Turning Basin (Scenarios 4a and 4b)

It is estimated that dredged volume along the approach channel and turning basin is approximately 1.07 Mm3 in total.  There are two dredging options which were defined as Scenarios 4a and 4b.  Figures A3.4 and A3.5 illustrate the location of the emission for these two options: 

·       Scenario 4a:  Deployment of 2 grab dredgers; and,

·       Scenario 4b:  Combination of 1 grab dredger and 1 TSHD. 

 

Deployment of Grab Dredgers (Scenario 4a)

Three grab dredgers will be used to dredge the material within Areas C and D (Figure A3.4).  On the same basis of the grab dredging of seawall, the emission rate of the grab dredgers is 1.97 kg s-1 (emitted continuously at the whole water column). 

A stationary emission point, SS03, is defined in the model to represent the grab dredgers for the jetty whereas SS04a and SS05 are chosen for Areas C and D (the approach channel and basin) respectively.  SS04a and SS05, which are also stationary points, are well represent the most conservative case in view of their proximity to the shore and hence the sensitive receiver, i.e., the coral habitat.  In reality, the grab dredgers will move around the approach channel and turning basin, i.e., farther away from the sensitive receiver, and hence less impacts to the coral are expected.

 

Combination of Grab Dredgers and TSHD (Scenario 4b)

As indicated in Figure A3.5, a TSHD (SS04b) will be used at Area C while two grab dredgers (SS03 and SS05) will be deployed at Area D.  The emission rate of the grab dredgers is 1.97 kg s-1 as discussed above.   

It is assumed that the TSHD will move at a speed of 0.3 m s-1 starting at utmost northeast of the approach channel along the direction of the channel.  The suggested size of trailer dredger is approximately 8,000 m3 and the effectively capacity is 5,400 m3, which commonly operate in Hong Kong.  The TSHD is expected to dispose of the material off-site, potentially at South Cheung Chau disposal site.  The number of trips per day varies depending on the distances between the working locations and the disposal site (Table A3.2).  For each trip, the dredging volume will be 7,200 m3, the most conservative case, lasting for approximately 45 minutes.  Based upon the loss rate assumption of 7 kg m-3, the calculated loss rate will be 18.67 kg s-1 (about 10% bottom of water column).

3.4.4                                Construction Works for Submarine Cable Installation (Scenario 5)

Grab Dredging

Dredging will be carried out at Shek Pik and South Soko shore Approach.  The dredging works for submarine cable will be done together with the dredging works for water main detailed in Section 3.4.2.  In Scenario 2, it has been conservative assumed that a 16 hour working day will be employed with a 6 day working week throughout the works.  Using the dredging rate of 8,000 m3 day-1 a continuous emission rate of 2.36 kg s-1 has been modelled throughout the whole water column. 

Jetting

Working hours have been assumed to be 12 per day.  One jetting machine, moving at speed of 150 m hr-1, will work along the cable alignment from Shek Pik to South Soko Island.  The dry density of sediment is assumed to be 700 kg m-3.  The submarine cable will be installed by direct burying with a rate of 150 m hr-1 per machine and thus the jetting rate will be 2,700 m3 day-1, which equates to a continuous emission rate of 8.75 kg s-1 (bed layer).  Figure A3.6 presents the start point of the moving source (SS14) and it will move seawards following the curb of the cable.

3.4.5                                Construction Works for Submarine Intake and Outfall (Scenario 5)

The approach is similar to that for seawall construction.  It is conservative to assume that two separate grab dredgers will be used for the dredging at the submarine intake and outfall locations respectively although the dredging works is likely to occur one followed one without overlapping.  Working hours have been assumed to be 24 per day.  The estimated dredged volume is approximately 0.03 Mm3 in total. 

As seen from Figure A3.6, a stationary point source at each of the intake (SS15) and outfall (SS28) will release at a continuous emission rate of 1.97 kg s-1. 

3.4.6                                Construction Works for Gas Receiving Station (Scenarios 6)

Scenario 6 simulates the concurrent dredging and sandfilling works at the GRS. 

Grab Dredging

Dredging volume is approximately 0.29 Mm3.  Working hours have been assumed to be 16 per day.  Assuming the deployment of two dredgers and  using the dredging rate of 8,000 m3 day-1 a continuous emission rate of 2.36 kg s-1 has been modelled throughout the whole water column.

In view of the small size of dredging area (covered by two grid cell in the model), two stationary emission points are defined (SS29 and SS30 shown in Figure A3.7). 

Sandfilling

Sandfilling for seawall trench and the reclamation at GRS by a pelican barge (rainbowing) is simulated by assuming a filling rate of 50,000 m3 day-1 with working hours to be 16 per day.  The fill material will be marine sand which generally has a fine content ranging from 2% to 10%.  As the source of material could not be confirmed at time of EIA compiled, the upper bound of the fine content, i.e. 10% is assumed for the conservative case.  The dry density of sand fill will be approximately 1,938 kg m-3.  A highly conservative loss rate of 10% is assumed, giving a rate of release of 16.8 kg s-1 (continuous in whole column).

Since the seawall trench and reclamation area is small and close to the shore which is covered by approximately one grid cells in the model, a stationary emission point, SS31, (Figure A3.7) has been chosen at a cell that well represents both the seawall trench and the reclamation.

3.4.7                                Construction Works for Gas Pipeline (Scenarios 7 to 13)  

The estimated dredged volume, the number of plant and the distance apart between each plant at the associated pipeline section is shown in Table A3.3.  The working hours have been assumed to be 24 per day for TSHD dredging and 12 hour per day for grab dredging.  The route is shown in Figure A3.8.

Table A3.3      Submarine Gas Pipeline Construction Details

Zone

(KP)

Scen-ario

Plant Used

Dredged Volume

(Mm3)

Moving Speed

(m h-1)

Number of Plant

Minimum Distance Apart between Each Plant (m)

South Soko Approach

(0-1)

7

Grab Dredger (a)

0.07

2.5

1

N/A

West of South Soko to West Lantau

(1-24.5)

8

TSHD (b)

1.28

33

1

N/A

Northwest Lantau to Urmston Road Crossing (24.5-31)

9

Grab Dredging (a)

0.17

2.5

3

2,167

Urmston Road Crossing (31-33.5)

10

Grab Dredging (a)

0.07

2.5

1

N/A

West of Black Point

(33.5-37)

11

Grab Dredger (a)

0.30

2.6

3

1,167

West of Black Point

(37-37.803)

12

Grab Dredger (a)

0.02

2.5

1

N/A

Black Point Shore Approach

(37.803-38.303)

13

Grab Dredger (a)

0.02

4.75

1

N/A

Notes:

(a)      Grab dredger denotes a closed grab with a minimum grab size of 8 m3.

(b)      TSHD denotes Trailer Suction Hopper Dredger with hopper capacity of 11,300 m3.

Combination of Grab Dredge and TSHD Dredging

Grab Dredging:  The dredging will be carried by one to three closed grab dredgers.  It is assumed that the grab dredging rate is 4,000 m3 day-1 for the pipeline dredging, which gives a loss rate of 0.79 kg s-1 per plant respectively throughout the whole water column.

 

TSHD Dredging:  The dredging will be carried by one TSHD.  It is assumed that the dredging rates are 7,200 m3 per trip and each dredging event lasts approximately 0.75 hour, which gives a loss rate of 18.7 kg s-1 for KP1 – KP24.5 respectively releasing at the bed layer (10% of the water column).

Alternative Gas Pipeline Route

Potentially, a container port, CT10, will be built to the west of Lantau (near Tai O).  If this is the case, it will hence be necessary to alter the LNG submarine gas pipeline in order to avoid the intersection with the CT10 which may require dredging the port area to substantial depth for reclamation.  An alternative pipeline route was designed to bypass the CT10.  To assess any potential impacts due to the alternative pipeline route was thus simulated by Delft3D model.   The modelling is mainly carried out for KP7 – 14, KP14 – KP20 and KP20 – KP34.5 since the changes are mainly at these three zones.  The model results are presented in Appendix 6C in this Annex.

3.4.8                                Construction Programme and Sequence

Tentative construction programme and indicative construction sequence are shown in Figures A3.9 and A3.10 respectively.


 

Figure A3.9    Tentative Construction Programme


3.5                                      Sewage Discharge

During construction of the LNG terminal the maximum work force is estimated to be around 1,600 people maximum.  Based on Table 2 of the Drainage Service Department’s (DSD’s) Sewerage Manual for domestic type sewage, the unit flow factor for an employed population is 150 L per head per day.  A calculation of the Average Dry Weather Flow (ADWF) is given in Table A3.4.  According to the Sewerage Manual, a peaking factor of 6 should be applied to the average flow to determine the peak flow which is also shown.

Table A3.4     Calculation of Sewage Flow LNG Construction Phase

Population

Unit Flow Factor

(L/head/day)

Average Dry Weather Flow (ADWF)

(m3/day)

Peak Flow

(6 x ADWF)

(m3/day)

1,600

Domestic Type

150 L/head/day

240

1,440

 

Total

240

1,440

From the above, the effluent discharge consent standard, based on the ADWF, can be obtained from Table 10a of the TM and is summarised in Table A3.5.  As the sewage from the LNG terminal at South Soko Island is of domestic sewage type, the parameters as shown in Table A3.5 are applicable to the sewage treatment process.  The other parameters that comprise restrictions on chemicals are not a concern for domestic type sewage and are therefore considered.  For oil and grease this requires to be controlled by fitting grease traps to the sewage outlets from the kitchens.  The design load of the sewage discharge is the same as the effluent discharge standard and also shows in Table A3.6.

Table A3.5      Effluent Discharge Standard and Design Load for the Sewage Treatment Works during Construction Phase

Site

Corresponding WCZ

BOD

(mg/L)

SS

(mg/L)

Total Nitrogen

(mg/L)

E.Coli

(count/100mL)

South Soko

Southern

20

30

100

1,000

3.6                                      Hydrotest Discharge

An assessment of the impacts from hydrotest discharges is required.  These tests are needed to check the integrity of the pipeline from Soko Island to Black Point.  In the freshwater testing additives are used.  At this stage an assessment of the initial dilution suffices because the discharge is relatively small and decay rates of the additives are unknown.  A most conservative approximation is thus applied because dilution only provides the upper bound of concentrations in the discharge plume.

3.6.1                                Discharge Location

There are two alternative locations where the hydrotest water will be discharged:

·       Black Point, where the hydrotest discharge water is combined with the existing thermal effluent flow from the Black Point Power Station; or

·       Soko Island, where the discharge is located at the south of Soko Island (proposed outfall).

3.6.2                                Discharge Rate

It is estimated that 20,000 m3 hydrotested water from the pipeline with a rate of 0.19 m3 s-1 will be discharged (last for about 1.2 days). 

3.6.3                                Modelling Approach

Near-field model, CORMIX, is used to investigate dilution of discharges in varying but steady state conditions for both the dry and wet seasons.  The area of the diluted plume (in terms of distance from the source) has been assessed.

 

 

4                                            Operational Phase

For the study of operational effects, the approach requires several steps:

1)  Running a near-field model (i.e. CORMIX) for the operational discharges to characterise the initial mixing of the effluent discharge.  The results of the near-field model has been used to define the manner in which the discharge would be included in the far-field hydrodynamic and the water quality models (at which depth, the number of cells over which the discharge will be distributed).  The results from the CORMIX analysis have also provided information of the near field dispersion and dilution of the effluent plumes and hence chlorine and/or other biocide concentrations.

     The details of CORMIX simulation is presented in Appendix B of this Annex.

2)  Adapting the hydrodynamic model for the new conditions, including the reclamations and discharges. 

3)  Running the hydrodynamic model for the specified conditions (wet/dry season).  Both sites can be implemented within one hydrodynamic run for a dry and wet seasons spring-neap cycle, since there will be no significant interaction between the effects of the two sites.

4)  Running the water quality model (i.e. Delft3D-WAQ).  The objectives are twofold:

a) to qualitatively assess the concentrations of residual chlorine or other biocides: to this end up to 5 decayable tracers may be defined, which will be released from the two candidate sites (the analysis has been carried out assuming that the background concentration is zero); and

b) to qualitatively assess the potential changes in water quality as a result of changes in the circulation near the project sites: to this end up to 5 conservative, i.e. non-decayable, tracers have been defined, which will be discharged from a number of locations representing main pollution sources (e.g. Hong Kong as a whole, major point sources in the vicinity of the candidate sites).

The general water quality is the result of transport phenomena and transformation and retention processes.  The operation of the project may locally affect the transport patterns.  Transformation and retention processes are not affected.  Consequently, validation of the Delft3D-WAQ model is not required.  The analysis under 4b) requires the running of a baseline scenario to assess the pre-project conditions.

4.1                                      Thermal and Antifoulant Discharge

Stored LNG will need to be re-gasified in order for it to be conveyed along the gas pipeline to the point of use.  Seawater discharged from the LNG terminal is expected to have a decreased temperature of approximate D 12.5°C at the discharge point.  The flow rate is expected to be equivalent to 18,000 m3 hr-1 (peak flow).

The dosing level of Chlorine is expected to be at approximately 3 mg L-1.  Residual Chlorine level is expected to be less than 0.3 mg L-1.  Hence 0.3 mg L-1 is simulated in the model for both maximum discharge flow and the seasonal varied discharge flow as shown in Table A4.1. 

Table A4.1      Cooling Water Discharge Flow Rate

Hour

Summer (m3 hr-1)

Winter (m3 hr-1)

0

13500

9000

1

13500

6750

2

11250

4500

3

11250

4500

4

11250

4500

5

11250

4500

6

11250

4500

7

11250

6750

8

15750

9000

9

18000

11250

10

18000

15750

11

18000

18000

12

18000

18000

13

18000

18000

14

18000

18000

15

18000

18000

16

18000

18000

17

18000

18000

18

18000

18000

19

18000

18000

20

18000

18000

21

18000

18000

22

18000

15750

23

15750

11250

Residual chlorine is known to decay rapidly in the marine environment, as the chlorine demand of the receiving waters is likely to be high.  A preliminary review of literature on chlorine decay has indicated that there are a number of factors that determine decay, including reactivity of organic matter, temperature, (UV) light, pH and salinity.  However, chlorine decay has been studied mostly for freshwater systems and in distribution system. 

Based on this review, a conservative rate of decay has been taken as first order decay (i.e., 100 day-1) at 30°C.  As chlorine will be discharged in cooled water from the gas warming vaporisation system, a similarly conservative temperature dependency of 1.0996 has been used in the modelling ([9]).

4.2                                      Sewage Discharge

During operation of the LNG receiving terminal the maximum work force is estimated to be around 100 people maximum.  Based on Table 2 of the Drainage Service Department’s (DSD’s) Sewerage Manual, the unit flow factor for an employed population is 60 L per head per day.

However, this unit flow rate does not comprise wastewater generated from staff showers or any canteen facilities to be provided.  Considering the nature of the work and remote locations, some of the work force may use shower facilities and also canteen facilities will be required.  In this case subject to discussion and agreement with Environmental Protection Department (EPD) a commercial unit flow factor may be applied to the work force on top of the employed population unit flow factor.  Table A4.2 shows a calculation of the Average Dry Weather Flow (ADWF) and the peak flow for which a peaking factor of 6 is applied.

Table A4.2      Calculation of Sewage Flow LNG Operational Phase

Population

Unit Flow Factor

(L/head/day)

Average Dry Weather Flow (ADWF) (m3/day)

Peak Flow

(6 x ADWF) (m3/day)

100

Employed Population

60L/head/day

6.0

36.0

100

Commercial Activities

29.0

174.0

 

Total

35.0

210.0

From the above, the effluent discharge standard, based on the ADWF, can be obtained from Table 10a of the TM and is summarised in Table A4.2.  As the sewage from the LNG Plant is of domestic sewage type, the parameters as shown in Table A4.3 are applicable to the sewage treatment process.  The other parameters that comprise restrictions on chemicals are not a concern for domestic type sewage and are therefore considered.  For oil and grease this requires to be controlled by fitting grease traps to the sewage outlets from the kitchens.  The design load of the sewage discharge is decided to be same as the effluent discharge standard.

Table A4.3      Effluent Discharge Standard and Design Load for the Sewage Treatment Works during Operational Phase

Site

Corresponding WCZ

BOD

(mg/L)

SS

(mg/L)

Total Nitrogen

(mg/L)

E.Coli

(count/100mL)

South Soko

Southern

20

30

100

1,000

4.3                                      Maintenance Dredging

The study has considered the following three steps that steer sedimentation.  Two types of material have been taken into account, i.e. mud (cohesive) and sand (non-cohesive).  Mud is transported in suspension and sand is transported as suspended load or bed load, depending on the grain size and wave/current conditions.

1)   To estimate the rate of sediment supply, data on bed composition in the vicinity of the LNG terminals (if available also sediment cores), data on suspended sediment concentration (preferably also during or just after typhoons) and data on the sediment load and the extent of the sediment transport of Pearl River has been analysed.  From the mineralogical composition, sediment sources can be identified. 

2)   The current velocity in and around the navigation channel and the resulting bed shear stress.  To this end, results from existing hydrodynamic model simulations can be used.

·       The influence of waves has been evaluated based on a combination of wave climate data analysis from measurements, existing wave model results and desk analysis.

·       An analysis of recirculation patterns by wind and tide to identify transport pathways.  The tidal excursion length is also an important parameter to consider.

·       Based on available data, it has been assessed what the effect of seasonal variations is and what the importance of density-driven effects is, e.g. salinity, fluid mud, temperature.

3)   From the analysis on sediment supply and transport, an estimate can be made on the sedimentation rate in the navigation channel and in the neighbourhood of the terminal.  From the average and maximum shear stress in the trench induced by currents and waves, the sediment trapping efficiency can be estimated.  The product of supply and trapping efficiency yields the sedimentation rate.

Following the above approach, the frequency of the maintenance dredging has been estimated.  For the impact assessment of the maintenance dredging, the qualitative assessment has been conducted (discussed in the Section 6 – Water Quality Impact Assessment) since the scale of the maintenance dredging would be much less than the dredging works for the approach channel and turning basin during construction phase which has been modelled as described in the previous section.

4.4                                      Accidental Fuel Spillage

4.4.1                                Locations

A release point (808503 easting, 801160 northing) is defined just in from the boundary of Hong Kong waters on the approach to the island.  This point is on the potential LNG carrier route and thus chosen for the impact assessment.  To be conservative, the release point is assumed to be just above the waterline.

4.4.2                                Fuel Type

Based on the information, it is assumed that the fuel is Heavy Fuel Oil (HFO i.e., 100% No 6).  

4.4.3                                Volume to be spilled

The most conservative case scenario was modelled, i.e. the largest single HFO storage tank from a 210 km3 SSD propulsion vessel which is 5,043 m3.  The inventory released should equate to 60% of the tank contents. 

4.4.4                                Discharge Rate

It is assumed the large carrier will be used and its large collision event has a release rate of 8,060 kg s-1, even though the small carrier will also be adopted in reality, giving a large collision event having a lower release rate of 7,720 kg s-1.

4.4.5                                Model Selection

The oil spillage has been simulated using hydrodynamic and particle tracking models (oil module of Delft3D-PART) to assess the movement of the oil spill.  This Delft3D-PART forms part of the well-calibrated Delft 3D suite of models, as described in Section 1 of this Annex.  This particle tracking model has been adopted in the EIA of Permanent Aviation Fuel Facility ([10]). 

4.4.6                                Key Modelling Assumptions

Fuel spill is modelled by surface particles (floating since the density of the oil is less than that of the water). The initial radius is calculated on the basis of the Fay and Hoult equation ([11]) that calculates the extent of the patch after gravitational spreading.  This spreading occurs in a matter of minutes rather than hours. The radius is related to the density difference between the oil and the water and the volume of spilled oil). The spill as used in the present case, of heavy fuel oil would lead to an initial patch of a diameter of 440 m.  This implies a thickness of about 5 mm. In addition, no evaporation rate and emulsification is assumed in the model. The wind data at Cheung Chau and Sha Chau as shown in Annex 13A3 in Section 13 is used in the model.

4.4.7                                Scenarios

The PART model has been simulated for the dry and wet seasons with typical real time wind time series. The simulations were run for periods of 5 days to capture the transport route of the oil spill in the first 24 hours to facilitate the development of an emergency contingency plan.


5                                            Cumulative Impacts

At present there are no planned projects that could have cumulative impacts with the construction of the terminal at South Soko and the gas pipeline. The construction of the HK-Zhuhai-Macau Bridge and potential Western Port Development (CT10) are unlikely to be carried out concurrently with the construction works of the gas pipeline.  With reference to the Project Profile for the Lantau Logistic Park (LLP), the exact layout of the proposed LLP reclamation is the subject of further study and will be confirmed by the detailed investigations which are ongoing. The way forward and construction programme of the LLP are also uncertain at this stage.  No other projects are planned to be constructed in sufficient proximity to the Project to cause cumulative effects.  In light of the above, cumulative impacts are not expected to occur. 

 

 

6                                            Input Parameters

6.1                                      Sediment Parameters

For simulating sediment impacts the following general parameters has been used:

·   Settling velocity – 0.5 mm s-1

·   Critical shear stress for deposition – 0.2 N m-2

·   Critical shear stress for erosion – 0.3 N m-2

·   Minimum depth where deposition allowed – 1 m

·   Resuspension rate – 30 g m-2 d-1

·   Wave calculation method – Tamminga

·   Chezy calculation method – White/Colebrook

·   Bottom roughness – 0.001 m ([12])

·   Fetch for wave driven erosion – 35 km

·   Depth gradient effect on waves - absent

The above parameters have been used to simulate the impacts from sediment plumes in Hong Kong associated with uncontaminated mud disposal into the Brothers MBA ([13]) and dredging for the Permanent Aviation Fuel Facility at Sha Chau ([14]).  The critical shear stress values for erosion and deposition were determined by laboratory testing of a large sample of marine mud from Hong Kong as part of the original WAHMO studies associated with the new airport at Chek Lap Kok.

7                                            Scenarios

7.1                                      Construction Phase

The scenarios are constructed in accordance with the tentative construction programme (Figure A3.9).  To simulate conservative worse cases potential concurrent activities would be simulated at the same time regardless the reality that they may not all occur simultaneously.

The proposed scenarios for the construction phase of the South Soko Option are presented in Table A7.1.  Table A7.2 summarises the inputs defined in the water quality model.


Table A7.1      Scenarios of the Construction Works for South Soko Option

Scenario ID

Tasks

Details of Construction Activities

No. of Plant

Plant Type

Code

Scenario 1

Seawall/Reclamation Areas

Grab Dredging underneath Seawall for Eastern Berth

(Area A)

1 no.

Grab Dredger

SS

 01

 

Seawall/Reclamation Areas

Grab Dredging underneath Seawall for Western Berth

(Area B)

1 no.

Grab Dredger

SS

 02

 

Seawall/Reclamation Areas

Sand filling Seawall Trench and Reclamation for the Western Berth

1 no.

Pelican Barge

SS

 32

Scenario 2

Submarine Water Main

Grab Dredging at South Soko Shore Approach

1 no.

Grab Dredger

SS

 06

 

Submarine Water Main

Grab Dredging at Shek Pik Shore Approach

1 no.

Grab Dredger

SS

 07

 

Submarine Water Main

Grab Dredging Waterway Crossing Sand Borrow Area & Marine Navigation Channel

1 no.

Grab Dredger

SS

 08

Scenario 3

Submarine Water Main

Post Trenching Jetting near South Soko

1 no.

Jetting Machine

SS

 09

 

Submarine Water Main

Post Trenching Jetting near Shek Pik

1 no.

Jetting Machine

SS

 10

Scenario 4a

Jetty Box

Grab Dredging at Jetty Box

1 no.

Grab Dredger

SS

 03

 

Approach Channel and Turning Basin

Grab Dredging at Approach Channel & TB at Area C

1 no.

Grab Dredger

SS

 04a

 

Approach Channel and Turning Basin

Grab Dredging at Approach Channel & TB at Area D

1 no.

Grab Dredger

SS

 05

Scenario 4b

Jetty Box

Grab Dredging at Jetty Box

1 no.

Grab Dredger

SS

 03

 

Approach Channel and Turning Basin

TSHD Dredging at Approach Channel & TB at Area C

1 no.

TSHD

SS

 04b

 

Approach Channel and Turning Basin

Grab Dredging at Approach Channel & TB at Area D

1 no.

Grab Dredger

SS

 05

Scenario 5

Submarine Cable Circuit

Submarine Cable Installation by Direct Burying (Jetting)

1 no.

Jetting Machine

SS

 14

 

Submarine Intake

Grab Dredging under intake

1 no.

Grab Dredger

SS

 15

 

Cooled Water Outfall

Grab Dredging under outfall

1 no.

Grab Dredger

SS

 28

Scenario 6

Gas Receiving Station

Grab Dredging at GRS

1 no.

Grab Dredger

SS

 29

 

Gas Receiving Station

Grab Dredging at GRS

1 no.

Grab Dredger

SS

 30

 

Gas Receiving Station

Sand filling Seawall Trench and Reclamation at GRS

1 no.

Pelican Barge

SS

 31

Scenario 7

Submarine Gas Pipeline

Grab Dredging at South Soko Shore Approach (KP 0 - KP 1)

1 no.

Grab Dredger

SS

 21

Scenario 8

Submarine Gas Pipeline

TSHD Dredging from Fan Lau Crossing to West Lantau (KP 1 - KP 24.5)

1 no.

TSHD

SS

 32

Scenario 9

Submarine Gas Pipeline

Grab Dredging from Northwest Lantau to Urmston Road Crossing (KP 24.5 – KP 31)

3 nos.

Grab Dredger

SS

 33

Scenario 10

Submarine Gas Pipeline

Grab Dredging across Urmston Road Crossing (KP31– KP 33.5)

1 no.

Grab Dredger

SS

 34

Scenario 11

Submarine Gas Pipeline

Grab Dredging at West of Black Point (KP33.5 – KP 37)

3 nos.

Grab Dredger

SS

 19

Scenario 12

Submarine Gas Pipeline

Grab Dredging at West of Black Point (KP 37 – KP 37.803)

1 no.

Grab Dredger

SS

 35

Scenario 13

Submarine Gas Pipeline

Grab Dredging at Black Point Shore Approach (KP37.803 - KP38.303)

1 no.

Grab Dredger

SS

 16

 

 


Table A7.2      Summary of Model Inputs

Code

Emission Point

No. of Working Plant

Dredging/Jetting/ Sandfilling Rate

Operation Duration

Loss Type

Loss Rate

Loss Rate

Input Layer

 

 

 

m3/day/plant

hours

-

kg m-3

kg s-1

-

SCENARIO 1

Dredging and Backfilling for Seawall

SS 01

Grab Dredging underneath Seawall for Eastern Berth

(Area A)

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 02

Grab Dredging underneath Seawall for Western Berth

(Area B)

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 32

Sand filling Seawall Trench and Reclamation for the Western Berth

1 X Pelican Barge

70,000

24

Continuous

1%

16.8

whole column

SCENARIO 2

Dredging for Water Main

SS 06

South Soko Shore Approach

1 X Grab Dredger (e)

8,000

16

Continuous

17

2.36

whole column

SS 07

Shek Pik Shore Approach

1 X Grab Dredger (e)

8,000

16

Continuous

17

2.36

whole column

SS 08

Waterway Crossing Sand Borrow Area & Marine Navigation Channel

1 X Grab Dredger (e)

8,000

16

Continuous

17

2.36

whole column

SCENARIO 3

Jetting for Water Main

SS 09

Post Trenching Jetting near South Soko

1 X Jetting

10,400

16

Continuous

20%

trench volume(b)

14.7

(1st pass)

29.5

(2nd pass)

44.2

(3rd pass)

bed layer (f)

SS 10

Post Trenching Jetting near Shek Pik

1 X Jetting

10,400

16

Continuous

20%

trench volume(b)

14.7

(1st pass)

29.5

(2nd pass)

44.2

(3rd pass)

bed layer (f)

SCENARIO 4a

Dredging for Approach Channel and Turning Basin

SS 03

Dredging at Jetty Box

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 04a

Dredging at Approach Channel & TB at Area C

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 05

Dredging at Approach Channel & TB at Area D

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SCENARIO 4b

Dredging for Approach Channel and Turning Basin

SS 03

South Soko Jetty Box

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 04b

Dredging at Approach Channel & TB at Area C

1 X TSHD

7,200 m3 per trip (a)

0.75

Piecewise

7

18.67

bed layer (f)

SS 05

Dredging at Approach Channel & TB at Area D

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SCENARIO 5

Jetting for Submarine Cable

SS 14

Submarine Cable Installation by Direct Burying (Jetting)

1 X Jetting

2,700

12

Continuous

20%

trench volume(c)

8.75

bed layer (f)

Dredging for Submarine Intake

SS 15

Dredging under Intake

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SS 28

Dredging under Outfall

1 X Grab Dredger (e)

10,000

24

Continuous

17

1.97

whole column

SCENARIO 6

Dredging/Backfilling for Gas Receiving Station

SS 29

Dredging for Gas Receiving Station (grab dredger 1)

1 X Grab Dredger (e)

8,000

16

Continuous

17

2.36

whole column

SS 30

Dredging for Gas Receiving Station (grab dredger 2)

1 X Grab Dredger (e)

8,000

16

Continuous

17

2.36

whole column

SS 31

Backfilling for Gas Receiving Station (grab dredger)

1 X Pelican Barge

50,000

16

Continuous

1%

16.8

whole column

SCENARIO 7

Dredging for Submarine Gas Pipeline

SS 21

Grab Dredging at South Soko Shore Approach (KP 0 - KP 1)

1 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

SCENARIO 8

Dredging for Submarine Gas Pipeline

SS 32

TSHD Dredging at Fan Lau Crossing (KP 5 – KP 6.84)

1 X TSHD

7,200 per trip (a)

0.75

Piecewise

7

18.7

bed layer (f)

SCENARIO 9

Dredging for Submarine Gas Pipeline

SS 33

Grab Dredging from West Lantau to Urmston Road Crossing (KP 24.5 – KP 31)

3 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

SCENARIO 10

Dredging for Submarine Gas Pipeline

SS 34

Grab Dredging across Urmston Road (KP 31 – KP 33.5)

1 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

SCENARIO 11

Dredging for Submarine Gas Pipeline

SS 19

Grab Dredging at West of Black Point (KP33.5 – KP 37)

3 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

SCENARIO 12

Dredging for Submarine Gas Pipeline

SS 35

Grab Dredging at West of Black Point (KP 37 – KP37.803)

1 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

SCENARIO 13

Dredging for Submarine Gas Pipeline

SS 16

Grab Dredging at Black Point Shore Approach (KP37.803 - KP38.303)

1 X Grab Dredger (e)

4,000

12

Continuous

17

1.6

whole column

Notes:

(a) For TSHD, with hopper capacity of 11,300 m3, the duration stated refers to the operation time per trip and each dredging event will last for around 0.8 hour.

(b) Jetting for water main, the trench cross-section area (m2) is (5+2)x5/2 = 17.5 m2.

(c) Jetting for cable circuit, the trench cross-section area (m2) is 5X0.3 = 1.5 m2. 

(d) Jetting for gas pipeline, the trench cross-section area (m2) is 5×3 = 15 m2. 

(e) Grab dredger refers to closed grab dredger with a minimum grab size of 8 m3.

(f) Bed layer refers to the bottom 10% of the water column.


 



([1])        ERM - Hong Kong, Ltd (2005) Detailed Site Selection Study for Proposed Contaminated Mud Disposal Facility within the Airport East/East of Sha Chau Areas.  Environmental Impact Assessment (EIA) and Final Site Selection Report.  For the Civil Engineering and Development Department, Hong Kong SAR Government.  Approved on 1 September 2005

([2])        ERM-Hong Kong, Ltd (2000) Construction of an International Theme Park in Penny's Bay of North Lantau together with its Essential Associated Infrastructures - Final EIA Report.  For the Civil Engineering and Development Department, Hong Kong SAR Government. Approved on 28 April 2000.

([3])        ERM - Hong Kong, Ltd (1997) Environmental Impact Assessment: Dredging an Area of Kellett Bank for Reprovisioning of Six Government Mooring Buoys.  Working Paper on Design Scenarios. For the Civil Engineering Department, Hong Kong Government.

([4])        EGS (Asia) Limited (2005) Ground Investigation. For CLP Power Hong Kong Limited.

([5])        ERM - Hong Kong, Ltd (1997) Op cit.

([6])        Kirby, R and Land J M (1991).  The impact of Dredging - A Comparison of Natural and Man-Made Disturbances to Cohesive Sedimentary Regimes.  Proceedings CEDA-PIANC Conference (incorporating CEDA Dredging Days), November 1991, Amsterdam.  Central Dredging Association, the Netherlands.

([7])        Environment Canada (1994).  Environmental Impacts of Dredging and Sediment Disposal.  Les Consultants Jaques Beraube Inc for the Technology Development Section, Environmental Protection Branch, Environment Canada, Quebec and Ontario Branch.

([8])        For Water Main: 65 m hr-1 × (1 ÷ 3600 s hr-1) × 17.5 m3 m-1 = 0.32 m 3 s-1;

For Cable Circuit: 150 m hr-1 × (1 ÷ 3600 s hr-1) × 1.5 m3 m-1 = 0.0625 m 3 s-1;

For Gas Pipeline: 21 m hr-1 × (1 ÷ 3600 s hr-1) × 15 m3 m-1 = 0.0875 m 3 s-1 when the gas pipeline trench is fully fluidised.

([9])        McClellan, John N., David A. Reckhow, John E. Tobiason, James K. Edzwald:  A Comprehensive Kinietic Model for Chlorine Decay and Chlorination Byproduct Formation, Department of Civil and Environmental Engineering, University of Massachusetts/Amherst,

http://www.ecs.umass.edu/cee/reckhow/publ/84/acschapter.html

([10])  Mouchel Asia Ltd (2002). EIA of Permanent Aviation Fuel Facility. For Airport Authority Hong Kong.  Final Report.

([11])  Fay, J. and D. Hoult, 1971. Physical processes in the spread of oil on a water surface, Report DOT-CG-01 381-A, U.S. Coast Guard, Washington, D.C.

([12])       The particular formulations used express the bottom roughness by the so-called Nikuradse roughness coefficient, which has the dimension m. (Nikuradse, J., 1932: Gesetzmassigkeiten der turbulenten Stromungen in glatten Rohren. Frosch. Ver. Deutscher Ing. No. 356.)

(2)         Mouchel (2002a). Environmental Assessment Study for Backfilling of Marine Borrow Pits at North of the Brothers.  Environmental Assessment Report.

(3)         Mouchel (2002b). Permanent Aviation Fuel Facility.  EIA Report.  Environmental Permit EP-139/2002.