| Place of Origin: | China |
| Brand Name: | CEC TANKS |
| Certification: | ISO 9001:2008, AWWA D103 , OSHA , BSCI |
| Model Number: | W20160705009 |
| Minimum Order Quantity: | 1set |
| Price: | $5000~$20000 one set |
| Packaging Details: | PE poly-foam between each two steel plates ; wooden pallet and wooden box |
| Delivery Time: | 0-60 days after deposit received |
| Payment Terms: | L/C,T/T |
| Supply Ability: | 60 sets per month |
|
Detail Information |
|||
Sludge is the most demanding common storage duty because it attacks a tank from three directions at once: chemically from a sulphide-bearing vapour space, mechanically from grit and settled solids, and operationally through frequent cleaning. A manufacturer who has only ever built water tanks will produce a tank that passes a hydrostatic test and then, within two or three years, shows corrosion at the liquid line, a scum ring at the top, and consolidated solids at the bottom that nobody can get out.
Shijiazhuang Zhengzhong Technology Co., Ltd. (Center Enamel) builds sludge tanks across the full range - primary, secondary, digested and industrial - and the specification conversation always starts with the sludge characteristics, because the coating, the mixing and the outlet geometry all follow from them.
Because the liquid is only part of the problem. Above the liquid, biological activity continues and generates hydrogen sulphide, which in a covered tank reaches concentrations that are both corrosive and hazardous - routinely tens to hundreds of ppm, and far higher in septic material. At the liquid line, oxygen, condensate and sulphide meet, which is why that band corrodes first. Below, solids consolidate into a layer with a density that can exceed 1.2 tonnes per cubic metre and resist pumping, while grit carried in with primary sludge abrades the floor during mixing. And the tank must be cleaned - a process that damages more linings than service does.
Four capabilities. First, coating selection made against the actual chemistry - including the willingness to say where a coating is not suitable, because hot concentrated caustic and fluoride-bearing streams attack the glass phase of an enamel coating. Second, mixing engineering: mixer type, power density and placement matched to the solids range, typically around 5-15 W/m3 for mixed liquor and higher for thicker material. Third, outlet and floor geometry designed against the measured rheology, not copied from a water tank. Fourth, integrated gas and odour management: covered tanks with venting, treatment routing and safe access, because entry into a sludge tank vapour space is a confined-space operation.
Ask questions that cannot be answered from a catalogue. What coating do you recommend for this analysis, and where would you not use it? What mixing power density do you propose, and how was it derived? What outlet size and floor geometry do you recommend against this sludge, and what happens after a week of no mixing? How is the vapour space protected, and what is the confined space entry arrangement? What is the cleaning method the tank is designed for? A manufacturer who answers these with calculations and references is demonstrating capability; one who answers with assurances is not.
| Design parameter | Typical value or range | Why it matters |
|---|---|---|
| Solids content | Varies by sludge type | Drives mixing power and outlet design |
| Mixing power density | 5-15 W/m3 for mixed liquor | Derived from the solids range, not from habit |
| Hydrogen sulphide | Tens to hundreds of ppm in the vapour space | Makes the vapour space corrosion-critical |
| Coating thickness | 0.25-0.45 mm fused enamel | Same surface in vapour space and immersion |
| Limitation to check | Hot caustic and fluoride attack the glass phase | Select coating from the sludge analysis |
| Consolidated sludge density | Can exceed 1.2 tonnes per cubic metre | Sets outlet and floor geometry |
| Capability | Water tank builder | Sludge-capable manufacturer |
|---|---|---|
| Coating selection | One system for all duties | Selected from sludge analysis, limits stated |
| Vapour space | Often unspecified | Treated as the corrosion-critical zone |
| Mixing | Catalogue unit if requested | Power density derived from solids range |
| Outlet | Standard nozzle | Sized and located against measured rheology |
| Gas and odour | Not in scope | Cover, venting and treatment as part of the design |
| Cleaning | Left to the operator | Designed method with stated limits |
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. Sludge storage tanks are supplied with coating selected against the sludge analysis including stated limits, mixing engineered to the solids range, outlet and floor geometry sized against the measured material, cover and venting with confined-space provisions, and a cleaning method with stated pressure and access limits in the handover documentation.
A sludge tank is specified by the questions the manufacturer asks you. If the first question is about diameter, you are buying a water tank with a sludge label on it.
A sludge analysis: dry solids content and its range, pH, temperature, sulphide or sulphate content, chloride content, grit content, and whether the sludge is primary, secondary, digested or industrial. Add the retention requirement and the downstream process. That dataset drives coating selection, mixing, outlet geometry and gas management; without it, the manufacturer has to guess.
For holding duties, yes in most cases. Without mixing, solids settle and consolidate, usable volume falls, and the material can become septic and difficult to pump. Intermittent mixing at around 5-15 W/m3 is typical for mixed liquor, with higher power density for thicker material. If the tank is genuinely a short-term buffer measured in hours, mixing requirements can be reduced, but that should be a deliberate decision.
It depends on the analysis. Glass fused to steel performs well in sulphide-bearing vapour and against grit and cleaning, which is why it is widely used. The boundary conditions to check are hot concentrated caustic and fluoride-bearing streams, which attack the glass phase. Where those are present, an alternative coating or material should be evaluated before ordering rather than after installation.
Yes. Volume and geometry, coating grade for the analysed sludge, mixer type and power, floor and outlet geometry, cover and venting with gas treatment routing, access and cleaning provisions, and structural design to the site wind and seismic conditions are all configured to the duty.