Tender For Overhauling Of Electrolyser 1Set (Consisting Of 3 Nos) At Stream-A In The Electro Chlorination Plant During Aoh 25-26
Tender Overview
Project Description
Tender For Overhauling Of Electrolyser 1Set (Consisting Of 3 Nos) At Stream-A In The Electro Chlorination Plant During Aoh 25-26; 1 Charges for removing the Busbar terminals in Electrolyzer both positive end and negative end separately, disconnect the vent lines/Hydrogen separator and its connected lines, removing 1 No Electrolyser with flow rate 51Kg/hr from bed and place it horizontally on the ECP working area, removing the top & bottom outer flange of Electrolyser, removing the titanium fin plates from the FRP chamber, removing guide vanes, PVC top & bottom plates, after removing inspection, high pressure water cleaning & complete acid cleaning Electrolyser including cost of consumables and T&P hire charges 2 Charges for Re-assembling the dismantled PVC top & bottom plates, guide vanes and the titanium fin plates in the FRP chamber, reassemble the top & bottom FRP outer flange of Electrolyser, re-erecting 1 No Electrolyser with flow rate 51Kg/hr in bed, reconnecting the Busbar terminals in Electrolyzer both positive end and negative end separately, Reconnecting the vent lines and its connected lines & commissioning, consumables, leading & lifting and T&P hire charges.
BOQ
| Sl. No. | Item Description |
| 1 | Charges for removing the Busbar terminals in Electrolyzer both positive end and negative end separately, disconnect the vent lines/Hydrogen separator and its connected lines, removing 1 No Electrolyser with flow rate 51Kg/hr from bed and place it horizontally on the ECP working area, removing the top & bottom outer flange of Electrolyser, removing the titanium fin plates from the FRP chamber, removing guide vanes, PVC top & bottom plates, after removing inspection, high pressure water cleaning & complete acid cleaning Electrolyser including cost of consumables and T&P hire charges |
| 2 | Charges for Re-assembling the dismantled PVC top & bottom plates, guide vanes and the titanium fin plates in the FRP chamber, reassemble the top & bottom FRP outer flange of Electrolyser, re-erecting 1 No Electrolyser with flow rate 51Kg/hr in bed, reconnecting the Busbar terminals in Electrolyzer both positive end and negative end separately, Reconnecting the vent lines and its connected lines & commissioning, consumables, leading & lifting and T&P hire charges. |
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Tender Published
Tender notice published.
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Online submission via eProcurement portal.
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Technical bids will be opened and evaluated.
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