Water treatment plant Payment method More buyer enquiries Home

Find below details of water treatment plant required by a company from Syria . Company details including email ,address, telephone number, name of contact person, for this specific enquiry and other requirements for water treatment & related products will be sent on subscription. Please email us or contact on 91-022-25664078/55554853 if interested. Details of buyer for a single enquiry are also available on payment of our nominal charges Contact us

Present activities: Water Treatment plant for Iraq

Buyer has already got the order. Buyer also has requirement for multiple water treatment packages.

SCHEMATIC BLOCK DIAGRAM OF WATER TREATMENT PLANT available as an MS Excel Sheet, click on link to open/download

1. Description of the Treatment Process

Sources of the raw water are the from river within the plant boundary. From these water will be pumped and pass through clarifier and stored in the new underground clarified water storage sump. Clarified water pump will pump the clarified water to the multi grade filter (MGF). Requisite alum and polymers are added before MGF. MGF will remove the suspended particles in the water. Activated carbon filter ( ACF ) will be connected in series with MGF to remove colour, odour, organics (if any) present in the water.

3.2 Sodium hypochlorite solution will be dosed at the inlet line to the clarified water tank for reducing the organics present in the water. This chlorination system consists of hypochlorite dosing tank and dosing pump.

3.3 Acid and antiscalant solution will be dosed at the outlet line of ACF for maintaining the pH and reducing the fouling effect present in the water respectively. This system consists of acid dosing tank and dosing pump, antiscalant dosing tank and dosing pump.

3.4 From the outlet of ACF, water will be passed through the cartridge filters for fine filtration. After fine filtration high pressure pumps will boost the pressure of the water to suit the RO membrane inlet.

3.5 In the RO membrane around 95% of the salts will get reduced and the permeate flow rate will be around 70%. RO permeate will be passed through a degasser for the removal of carbon dioxide present in the form of an acid in the permeate. Post chlorination and pH adjustment of the RO product water will be done using dosing systems containing dosing tanks and dosing pumps. Degassified water collected in the RO product water storage tank will be further softened in softener ( Na cation exchanger ). Soft water is collected in the soft water storage tank. Soft water transfer pumps will pump the soft water to make for the auxiliary boiler.

3.6 A portion of the degassified RO water from the outlet of the feed pumps after chlorination will be sent to the potable/ service water system network.

All piping will be UPVC for raw water supply lines in accordance with ISO standards. Piping for RO water, soft water be UPVC. High pressure lines for RO skid will be SS316. Piping for alkali and acid will be as per water treatment subcontractor. Potable water piping will be of UPVC.

The general operation of the plant is manual

1. Arrangement / Layout

Filters, RO skid, Ion exchangers, chemical solution tanks and chemical dosing pumps will be located indoors. Degasser tower, RO water tank, soft water tank, bulk chemical tanks and pumps will be located outdoors under a shed as a semi-outdoor construction

Schematic block diagram with ratings /size available Click here for BLOCK DIAGRAM

	Annex-1 Raw water requirement
		Continuous ( Max.)		Intermittent ( Max.)		Remarks
		m3/h	m3/day	m3/hr	m3/day
A	Vendors requirement
	Westfalia	17.4	417.6	--	--

	GT compressor cleaning ( Off line washing )	--	--	0.8	2.4	3 GT scheduled for one day
	GT turbine cleaning ( Off line washing ) per GT	--	--	22.8	68.4	3 GT scheduled for one day
	Closed circuit cooling water	--	--	--	0.32	20 Lit/GT

B	Water treatment plant reject
					300
C	Colony water requirement	--	--	--	15	150 lit/day/person

D	Plant Service water
	Work shop -Air washer system	--	--	3	3
	House keeping, irrigation	--	--	10	10
	Unforseen consumption	--	--	7	20
E	Auxiliary boiler - Steam system make-up	4.1	97.86	--	--	25 % condensate loss and 5.5 % flash steam

	Total	21.48	515.46	43.6	419.12

	Total instantaneous water requirement	65.0775	934.58

Gross raw water requirement considered as 1000 m3/day.

ANNEX - 2

DESIGN RAW-WATER ANALYSIS

SL. No.	PARAMETER	CONCENTRATION (Max.)
1.	pH	8.2
2.	Turbidity (NTU)	66
3.	Suspension (mg/l)	43
4.	Calcium as CaCO₃ (mg/l)	82
5.	Magnesium as CaCO₃ (mg/l)	39
6.	M Alkalinity as CaCO₃ (mg/l)	100 *
7.	Chlorides as CaCO₃(mg/l)	193
8.	Sulphate as CaCO₃(mg/l)	385
9.	Silica as SiO₂ ( mg/l)	3.3
10.	Total dissolved solids (mg/l)	930

Home Summary of buyer enquiries Free Trade Leads - Supplier Offers Send your feedback

Receive payment from your customers Check prices Importers, buyers, dealers, distributors, agents email lists