The TPSTW Stage V
project comprises the expansion and modification of the existing Stage I/II
works and Stage IV works of the TPSTW (there is no Stage III works). uUpon completion of the
Project the capacity of the STW would
be increased from the present daily average flow of 88,000 m3/day to
130,000 m3/day.
(a) Additional inlet and preliminary treatment works;
(b) Additional primary clarifiers;
(c) Additional secondary treatment facilities (new bioreactors and final clarifiers);
(d) Modification of existing bioreactors;
(e) Reconstruction of existing final clarifiers;
(a)
Additional inlet and preliminary treatment works;
(a)
Additional primary clarifiers;
(f) Disinfection facilities;
(g) Additional sludge treatment facilities; and
(h) Ancillary works to existing treatment facilities.
· Population
With reference to Population information is based
on the Projections of Population Distribution 2003 –
2012 prepared by Planning Department., tThe 2012 projected
population of the
catchment of TPSTW is 282,945.
· Flows
According to the projected population, the design
flow is estimated to be 100,000 m3/d. With a
reserve capacity of 30% for future development, the TPSTW Stage V project is
designed to cope with 130,000 m3/d and the Project will be implemented in 2
phases.
The
design capacity
capacities of
Phase 1 and Phase 2 works are 100,000 m3/d and 130,000 m3/d
respectively.
· Loads
The design load concentrations to be adopted by DSD are summarized as flows:
Pollutants |
Load (tonnes/d) |
Concentration (mg/l) |
BOD5 |
33.8 |
260 |
TSS |
45.5 |
350 |
TKN |
6.5 |
50 |
NH3-N |
3.64 |
28 |
|
Current Standards |
New Standards |
||||
95 percentile |
Maximum |
95 percentile |
Maximum |
Annual Average |
Monthly Geometric Mean |
|
BOD5 (mg/l) |
20 |
40 |
20 |
40 |
- |
- |
TSS (mg/l) |
30 |
60 |
30 |
60 |
- |
- |
Total N (mg/l) |
25 |
50 |
- |
35 |
20 |
- |
NH3-N (mg/l) |
- |
- |
- |
10 |
5 |
- |
E. coli (counts/ 100ml) |
- |
- |
15,000 |
- |
- |
1,000 |
The key
elements of the Phase 1 works (design capacity up to 100,000 m3/d)
include:
(a)
Additional inlet and
preliminary treatment works;
(b) Modification of existing secondary treatment process units (retrofit existing bioreactors and adding 2 new final clarifiers);
(c)
Reconstruction
of 6 existing final clarifiers;
(a)
Additional
inlet and preliminary treatment works;
(d)
Additional
sludge treatment facilities; and
(e)
Ancillary
works to existing treatment facilities.
The key elements of the Phase 2 works (design capacity up to 130,000 m3/d)
include:
(a) Construction of additional secondary treatment process units (1 primary clarifier, 3 bioreactors and 2 final clarifiers);
(b) Reconstruction of 4 existing final clarifiers;
(c) Disinfection facilities;
(d) Additional sludge treatment facilities; and
(e) Ancillary works to existing treatment facilities.
2.6.2 Disinfection will be achieved by ultra-violet irradiation. It is noted that consideration may be given to the use of chlorination for the Shatin STW, in which case there may be scope to include the Tai Po STW effluent as well. This scenario, should it transpires, is to be considered as part of any necessary studies for the chlorination.
(a) North District and Tolo Harbour Sewerage Master Plans (SMP);
(b) Review of North District and Tolo Harbour Sewerage Master Plans;
(c) Performance Verification of Discharge into Victoria Harbour from Tolo Harbour Effluent Export scheme, and
(a)
Harbour Area Treatment Scheme.
(d)