Stand Bid Pres
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Transcript of Stand Bid Pres
7/28/2019 Stand Bid Pres
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• STANDARD PROCEDURES
FOR BID PREPARATIONAND PROJECT REALIZATION
• EXAMPLE OF AN INTERNATIONALLY
FINANCED WWTP -
• ECI-Sinotrust Business Consulting Co., Ltd.
• Tel: 86-10-6773 8115/6/7
• Fax: 86-10-6773 8119
• E-mail: [email protected]
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Table of Contents
• Project Introduction
• Tendering Conditions
• Bid Consortium• Process and Plant Design
• Equipment List
• Bid Price• Internal Evaluation Result
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Project Introduction
– Project: Dairy Waste Water Treatment
– Financing: European Community
– Eligible Companies: European and Chinese
– Consultant: Danish
– Project Owner: Ministry of Agriculture
– Project Location: Five Different Sites in
Different Provinces
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Tendering Conditions
• Complete Design
• Equipment Procurement
• Turnkey Supply, Erection and Startup
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Bid Consortium
• Due to the tender’ s character and relatedcompetition structure a German-Chinese
consortium between the following parties has
been set up:
– General Machinery Engineering Co., Ltd.: Leader
– IfU Dr. Bernd Diering GmbH: Design
– ECI Sinotrust Co., Ltd.: Project Management
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Bid Price
• ECI used all available relationships to
research and verify the likely successful bid price.
• It turned out that the price was dominated
by Chinese procurement prices.• Simultaneously it could be established that
no references for Chinese competitors are
existing.• The Chinese competition seemed to be
decisive but not ideally equipped to do the
job.
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Internal Evaluation Result
• Bidding Participants: 26 among them
4 Europeans, 2 Joint Ventures
• First Ten Companies: All Chinese
• European Companies: 14th, 16th and 17th
• ECI Position: 13th bef. evaluation
• 1st
aft. evaluation
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Waste Water Treatment Plants Principle Design Features and Comments
• 1. The Dairy Waste Water
• 2. The Treatment Process
• 3. Sludge Treatment
• 4. Plant Design
– 4.1 Storage Basin
– 4.2 Adsorption Stage (A-stage)
– 4.3 Activated-Sludge-Stage (B-Stage)
– 4.4 Sludge Treatment
– 4.5 Dosing Plant
• 5. Operation Costs
• Price Sheet
• Design Drawing
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1. The Dairy Waste Water
– For treatment and purification of the waste water thefollowing aspects generally should be taken into
account:
– 1). Rainwater and cooling water should be
discharged through separate drainage systems.
– 2). An equalising storage tank is definitely to be
recommended. This facilitates biological treatment.
– 3). Fat and other floatable solids should be
separated in a first step before further biological
treatment.
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2. The Treatment Process
• The treatment is designed as a two stage activated sludge process
generally known as AB-process. Its basic function is as follows: – - In the first high-load stage (A-stage) pollutants are predominantly bound
into the activated sludge by adsorption.
– - In the second low-load stage (B-stage) the waste water is purified by
biological degradation.
• Typical for the AB-process are the following principles:
– - observance of a high sludge range in the A-stage (maximum load
activation) with SR greater than 2 kg BOD/(kg MLSS x d)
– - separation of the biocenosis of the respective stage
– - possible varying operational methods in the A-stage, i.e. aerobic or facultative anaerobic operational methods adapted to the sewage water
ingredients
– - process engineering generally without preliminary treatment in order to
maintain better utilization of the microbiological reaction mechanism.
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Advantages of AB Process Compared With
Other Process
• Economy:
– Investment savings > 30 %
– Energy savings up to 50 %
– Space reduction up to 50%
• Technology
– Less sensitive to peak loads such as pH, COD, BOD5,
nitrogen, etc. The high-load A-stage receives a 50 to 100 x
higher organic load than a conventional activated sludge
stage.
– Better and more balanced results can be reached with a
multistage process system than with a one stage system.
– A continuously operating system that is constantly
supported and inoculated externally shows a high process
stability.
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3. The Sludge Treatment
– Two treatment methods are planned:
• After dewatering by sedimentation in a prethickener to
reduce volume, the thickened sludge can be treated
aerobically or anaerobically.
– Normally aerobic sludge treatment is used for small plants with
small amounts of sludge. Regarding the energy demand in case
of bigger plants with corresponding high amounts of sludge
anaerobic sludge treatment with gas generation in a digester is
recommended. – Organic sludge components are reduced 50% leading to a sludge
mass reduction of up to 35 % after aerobic or unaerobic treatment.
The treated sludge flows into the post-thickening tank, also used
as storage tank with a storage time of more than 10 days.
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4. Plant Design4.1 Storage Basin
• The dairy’ s waste water is discharged
discontinuously. Hence incoming water is stored in
an equalizing basin and storage tank. From here the
treatment stages A and B are fed continuously by a
pumping station. The installed stirrers insure mixing
of incoming waste water.
• The storage basin can be operated in the following
ways:
– - Storage of waste water up to 12 hours
– - Pretreatment under anaerobic conditions by addingexcess sludge from A- and B-stage
– - Usage as a flocculation and flotation tank
– - Regulation of pH-value
– - Storage of the process water from sludge treatment
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4.2 Adsorption Stage (A-stage)
– The A-stage is a high load biological actived sludge stage with an anoxic-
oxic-tank and intermediate sedimentation tank. The pollutants are adsorbed
to the actived sludge and removed by taking off excess sludge. In addition to
that the effect can be intensified with precipitation dosing.
• 4.2.1 High-loaded-stage (Anoxic-oxic-tank)
– The high-loaded-stage is calculated with contents of MLSS = 2.5 kg m
– On the bottom of the activated sludge basin a fine bubble aeration andoxygen sensor is constructed with membrane plate diffusers.
• 4.2.2 Intermediate Sedimentation
– The intermediate sedimentation tank is a hopper-bottomed-tank without
scraper bridge. The intermediate sedimentation-tank has a low surface load
of less than 1.8 m/h. That insures are very good sedimentation.
– The purified water flows through an outlet trough. The activated sludge
sinks down and is collected in the cone. The return-sludge is conveyed
continuously back into the anoxic-oxic-tank.
– The excess activated sludge of the A-stage is pumped to the prethickening
tank.
4 3 A ti t d Sl d St (B St )
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4.3 Activated-Sludge-Stage (B-Stage)
• 4.3.1 Activated-sludge-tank
– The activated-sludge-stage is designed for biological removing of pollutants as
substrate and get nearly mineralised. The tank volume of the activated-sludge-stage therefore is much bigger than the volume of the A-stage.
– The low sludge load ratio is absolutely necessary to avoid bulking sludge and
filamentous bacteria.
– In the activated sludge stage carbon compounds are oxydised completely. The
nitrogen compounds are mostly nitrified to nitrate-nitrogen (NO3-N). To avoiddisturbance by scum the aeration in the low-loaded-stage is switched off from
time to time for denitrification.
– In the activated-sludge-tank a fine bubble membrane aeration and oxygen tube
measuring is installed.
• 4.3.2 Final Sedimentation Tank – The final sedimentation tanks are designed like the intermediate sedimentation
tank.
– Only the return sludge pump is a bigger one. The excess sludge will be
conveyed to the storage tank by opening a valve or by pumping it directly to the
prethickening tank.
4 4 Sl d T t t
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4.4 Sludge Treatment
• 4.4.1 Static Dewatering of Excess Sludge (Prethickening Tank)
– The excess sludge of the B-stage is normally pumped to the storage tank
and flows together with the raw waste water into the A-stage.Alternatively it is possible to pump the excess sludge directly into the
prethickening tank.
– After prethickening the DS-content is about 35 kg/m
• 4.4.2 Additional Sludge Treatment
– Sludge Digestion
» Dewatered sludge is conveyed into the digesters. Additionally sludge
inside the digester is recycled from bottom to top and heated by a
heat exchanger up to temperatures of 37C so as to guarantee bestconditions for digestion. The process is monitored by temperature
check and pH-sensor.
– Aerobic Sludge Treatment
» In the tank a fine bubble membrane aeration is installed as well as 2
stirrers to insure circulation while aeration is turned off.
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• 4.4.3 Treated Sludge Dewatering and Storage Tank
(Post-Thickening Tank)
– The digested sludge flows directly into the post-thickeningand storage tank. After dewatering by sedimentation the
DS-content is about 40 kg/m
• 4.4.4 Mechanical Thickening
– The mechanical thickening process consists of onecentrifuge including charging pumps and coagulant dosing
station.
– Coagulants for sludge conditioning are supplied dry and
processed with water. The coagulant agents are fed with a
dosing pump into the charging pipe to the dewateringstation.
– The extracted water is recycled into the waste water
storage tank. The dewatered sludge will be stored in
containers and discharged fore agricultural utilization.
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4.5 Dosing Plant
• Generally speaking the treatment plant works without any
dosing of chemicals. Temporarily it can be useful to
support biological processes.
• The dosing plant contains an equipment for adding of
– Iron chloride (FeCl3)
– Iron chloride is kept in liquid form and may be added into the
» storage tank ; inlet pipe to the A-Stage ; inlet pipe to the B-
Stage
– Acid:
» Acid is used in small amounts in case of very high pH-valuesin the raw waste water-inlet of the storage tank.
– Flocculates:
» Flocculates support the biological treatment and improve the
sedimentation of activated sludge- storage tank or inlet to the
B-Stage.
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• Energy costs are mainly expenditures for electricity
supply.
Costs for additives are minimal due to the characteristics
of the AB-process. Small amounts of acid might be addedtemporarily for the regulation of the pH-value.
Additionally iron compounds or flocculates might be
added from time to time. Occuring costs are minimal and
therefor irrelevant.
Service/Maintenance costs are minimized by the
reduction of mechanical installations. For the plant
operation not more than one or two staff are sufficient.
5. Operation Costs
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pos. description WWTP and engine house flat price total
1 excavation 3,925.00 m³
2 subconcrete 1520.00 m²3 filler concrete 150.00 m³
4 concrete for bottom, incl. form work, d = 0.40 m 610.00 m³
5 strip foundation, incl. form work 40.00 m³
6 concrete for walls, incl. form work 950.00 m³
7 roof covering, incl. form work 190.00 m³
8 roof balustrade 38.00 m³
9 gangway incl. balustrade 901.00 m³
10 steel and reinforcement 235.00 to
11 floor covering, d approx. 10 cm 67.10 m³12 industrial coating, floor 671.00 m²
13 structure of roof incl. covering.. 671.00 m²
14 partition walls, h=3.90m 180.00 m²
15 foundation grounding 380.00 m
16 foundations for pumps 8.00 m³
17 expansion joints 100.00 m
18 expansion joints 240.00 m
19 high windows, h=1.00 m, l ca. 65.00 m 65.00 m²
20 outside door, 2.25 x 1.01 4.00 pieces
20 double door, 3.00 x 1.50 1.00 piece
20 double door, 4.00 x 3.50 1.00 piece
20 roll-fronted door, 3.50 x 3.50 1.00 piece
21 interior doors
0.75x2.25 2.00 pieces
0.88x2.25 4.00 pieces
22 wall coating, h = 3.90 m 625.00 m²
amount
Specification for the project of Heilongjiang (civil works)
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pos. description WWTP and engine house flat price total
1 sewage pumps Q = 50 - 70 m³ / h 2.00 pieces
gate valve DN 100 4.00 pieces
backflow trap DN 100 2.00 pieces
emptying nozzle 2'' with ball valve 2.00 pieces
flexible joint assembly DN 100 2.00 pieces
flange couplings DN 100 4.00 pieces
fixed flange DN 100 2.00 pieces
lapped welding flange DN 100 8.00 pieces
flange connection 6.00 pieces
pipeline, DN 100 20.00 m
arc, 90° 6.00 pieces
branch, 100 / 100 2.00 pieces
pressure gauge 2.00 pieces
2 return sludge pump A-stage 30-50m³ /h 1.00 piece
gate valve DN 100 2.00 pieces
backflow trap DN 100 1.00 piece
flexible joint assembly DN 100 2.00 pieces
fixed flange DN 100 2.00 pieces
flange couplings DN 100 1.00 piece
flange connection DN 100 1.00 piece
lapped welding flange DN 100 2.00 pieces
emptying nozzle 2'' with ball valve 1.00 pieces
pressure gauge 1.00 piece
pipeline, DN 100 25.00 m
Arc, 90° DN 100 6.00 piecesreturn sludge pump B-stage 50-100 m³ /h 2.00 pieces
amount
Specification for the project of Heilongjiang (technical equipment)
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pos. description WWTP and engine house flat price total
control cabinet ca. 25.00 pieces
oxygen measurement 3.00 pieces
pH measurement 1.00 piece
temperature measurement 3.00 pieces
pressure measurement 4.00 pieces
level measurement 4.00 pieces
indoor lighting 30.00 pieces
outdoor lighting 20.00 pieces
flow meter, DN 100 3.00 pieces
on-site control incl. outdoor Box 35.00 pieces
pilot and control cable 5,000.00 m
PVC-insulated power cables 4,000.00 m
switches, 220V 30.00 pieces
power point 40.00 pieces
combination power point 10.00 pieces
outdoor terminal box 35.00 piecescommunication center 1.00 piece
fault indicator light and horn hooter 2.00 pieces
cable canal, b = 0.30 m 60.00 m
main wire 10.00 m
automation technology for blowers and pump (SPS) 1.00 psch
visual process guiding system 1.00 piece
heating 170 kW, gas 1.00 piece
amount
Specification for the project of Heilongjiang (electronical tech)
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ECI SINOTRUST
Process Flow chart
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ECI SINOTRUST
Pipe and Instrumentation Diagram
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ECI SINOTRUST
Ground Plan and Section
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ECI SINOTRUST
Digester Ground Plan and Section