| Place of Origin: | China |
| Brand Name: | CEC TANKS |
| Certification: | ISO 9001:2008, AWWA D103 , OSHA , BSCI |
| Model Number: | W |
| Minimum Order Quantity: | 1set |
| Price: | $5000~$20000 one set |
| Packaging Details: | PE poly-foam between each two steel plates ; wooden pallet and wooden |
| Delivery Time: | 10-30 days after deposit received |
| Payment Terms: | L/C,T/T |
| Supply Ability: | 60 sets per month |
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Detail Information |
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| Place of Origin | China | Brand Name | CEC TANKS |
|---|---|---|---|
| Certification | ISO 9001:2008, AWWA D103 , OSHA , BSCI | Model Number | W |
| Tank Body Color: | Dark Green / Can Be Customized | Corrosion Integrity: | Excellent |
| Steel Plates Thickness: | 3mm To 12mm , Depends On The Tank Structure | Chemical Resistance: | Excellent |
| Size Of Panel: | 2.4M * 1.2M | Easy To Clean: | Smooth, Glossy, Inert, Anti-adhesion |
| Highlight: | Glass fused steel sludge tanks,Septic condition holding tanks,Odorless sludge storage tanks |
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A sludge holding tank sits between two processes that never run at the same speed. The treatment plant produces sludge continuously or in batches, and the dewatering or digestion plant accepts it on its own schedule, with its own downtime, and occasionally with no notice. Somewhere in between there has to be a vessel that absorbs the mismatch - and the failure of that vessel is not a leak, it is a smell, a blocked draw-off, or a tank half full of material that has gone septic and can no longer be pumped.
Engineered by Shijiazhuang Zhengzhong Technology Co., Ltd. (Center Enamel), glass fused to steel sludge holding tanks are built for that in-between duty: a surface that resists the sulphide-bearing vapour above the liquid and the abrasion of grit below it, with the mixing, draw-off and access arrangements designed as part of the tank rather than bolted on later.
A sludge holding tank is a buffer, not a store. Its job is to accept sludge at 2-8% dry solids from primary clarifiers, DAF units or a digester, hold it for hours to a few days, keep it homogeneous enough to pump, and deliver it to the next process on demand. Design drivers are therefore hydraulic retention measured in hours, mixing power of roughly 5-15 W/m3 for mixed liquor and higher for thicker sludges, and a draw-off that will not bridge or rathole. A tank sized only by volume without checking mixing and outlet behaviour will stratify within a day.
Sludge is a three-phase material - water, solids and gas - and every one of those phases attacks the tank differently. Water loads the shell hydrostatically. Solids settle, abrade and consolidate into a layer that can exceed 1.5 tonnes per cubic metre. Gas generated by ongoing biological activity collects in the vapour space at hydrogen sulphide concentrations that routinely reach 50-500 ppm and, in septic sludge, several times that. A coating chosen only for immersion service will pass a water test and fail in the vapour space, which is where most holding tanks actually corrode first.
Glass fused to steel is a steel plate with a vitreous enamel coating fused at 820-930 degrees Celsius to a finished thickness of 0.25-0.45 mm, giving a surface rated at about 6.0 Mohs with adhesion around 3450 N/cm2 and holiday tested at 1500 V across the full surface. It is inert to the sulphide-bearing vapour that eats organic linings, hard enough to tolerate grit and controlled cleaning, and smooth enough that consolidated sludge releases from the wall rather than bonding to it. The limitation to state plainly: hot concentrated caustic and fluoride-containing streams attack the glass phase and must be checked before GFS is specified.
| Design parameter | Typical value or range | Why it matters |
|---|---|---|
| Solids content | 2-8% dry solids | Sets mixing power, outlet size and pumpability |
| Mixing power density | 5-15 W/m3 | Keeps solids suspended without shearing the material |
| Retention time | Hours to a few days | Beyond about 48 hours septicity risk rises sharply |
| Coating thickness | 0.25-0.45 mm fused at 820-930 degrees Celsius | Vapour space and immersion share one surface |
| Limitation to check | Hot concentrated caustic and fluoride attack the glass phase | Confirm sludge chemistry before specifying |
| Duty | Water Storage | Sludge Holding |
|---|---|---|
| Contents | Single phase, stable | Water + solids + generated gas |
| Design retention | Days to weeks | Hours to a few days |
| Mixing | None required | 5-15 W/m3, intermittent or slow continuous |
| First corrosion point | Immersion zone | Vapour space and liquid line |
| Main failure mode | Gradual coating ageing | Septic sludge, blocked draw-off, odour |
| Cleaning | Occasional | Scheduled, and a primary wear mechanism |
Every tank delivered by Shijiazhuang Zhengzhong Technology Co., Ltd. (Center Enamel) is engineered against AWWA D103-09 and EN 1090 with finite element verification of shell, roof and nozzle loads, fused at 820-930°C under ISO 9001 and ISO 45001 control, holiday tested at 1500 V across one hundred percent of the surface, and assembled with Grade 8.8 bolts and manufacturer-certified sealant. Holding tanks are supplied with mixer type and power matched to the actual solids range, outlet and cone geometry sized against the measured sludge rheology, vapour space ventilation and H2S provisions, and access for the cleaning method the plant will actually use.
The holding tank is the one vessel in a sludge line where doing nothing for twelve hours is a design failure. Size it for retention, then prove the mixing and the outlet before you sign the volume off.
For undigested primary sludge, holding beyond roughly 24-48 hours without mixing or cooling risks septicity: gas production rises, pH drops, and dewaterability suffers. Digested sludge is more stable but still stratifies. If the plant genuinely needs multi-day buffer capacity, the tank should be specified with continuous slow mixing and gas collection rather than as a passive vessel.
For odour control, yes in most jurisdictions, and for safety if the vapour space can accumulate hydrogen sulphide. A flat or domed cover with a vent routed to a treatment unit is standard. Where a cover is fitted, the vapour space becomes the corrosion-critical zone and the coating, sealants and any internal steelwork must be selected for it.
The vapour space needs the same inert surface as the immersion zone, not a cheaper atmospheric paint. On a glass fused to steel tank the plates are coated before assembly, so the vapour space has the same fused coating. Sealant and fastener specification then becomes the weak link and should carry its own chemical resistance statement.
Yes. Capacity, diameter and height, cone or flat floor, mixer type and power, outlet size and number, vortex or anti-settling arrangements, cover and venting, coating grade for the measured chemistry, and access for the intended cleaning method are all configured to the sludge characteristics and the site.