| Place of Origin: | China |
| Brand Name: | CEC TANKS |
| Certification: | ISO 9001:2008, AWWA D103 , OSHA , BSCI |
| Model Number: | W20161227006 |
| 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 |
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Detail Information |
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A UASB reactor is not a tank that happens to make biogas - it is a hydraulic machine whose entire performance rests on keeping a bed of granular sludge suspended in an upward flow, while the gas those granules produce is separated from the liquid and the solids before any of it leaves the vessel. Get the upflow velocity right and the bed fluidises gently and retains biomass measured in tens of grams per litre. Get it wrong and the granules either settle into a dead mass or wash out with the effluent, and the reactor's treatment capacity disappears in a matter of days.
Shijiazhuang Zhengzhong Technology Co., Ltd. (Center Enamel) supplies UASB reactors as engineered vessels, which means the internal hydraulic components - inlet distribution, three-phase separator and gas collection - are part of the tank design rather than something resolved on site.
UASB - upflow anaerobic sludge blanket - is a high-rate anaerobic process in which wastewater flows upward through a blanket of biologically active granules. Unlike a continuously stirred digester, there is no mechanical mixing: the upflow velocity and the gas produced by the granules provide all the contact. Biogas rises, liquid and gas separate in a three-phase separator at the top, and treated effluent leaves over a weir. Volumetric loading is high - commonly 5-15 kg COD per cubic metre per day for readily degradable industrial effluent, with hydraulic retention measured in hours rather than the 20-40 days typical of a mesophilic agricultural digester.
Four parameters, in order: upflow velocity, organic loading rate, temperature, and the influent's suitability for granulation. Upflow velocity at the top of the reactor is typically held around 0.5-1.2 metres per hour - high enough to expand the bed and improve contact, low enough that granules are not carried into the separator. Loading rate must match the wastewater's degradability, because overloading acidifies the bed within days. Temperature governs kinetics; mesophilic operation at 35-38 degrees Celsius is standard and a drop of a few degrees measurably reduces removal. Finally, not every wastewater granulates well: high suspended solids, fats, oils and grease, and inhibitory compounds all interfere.
UASB suits soluble, readily degradable, warm industrial effluent - food and beverage, distillery, brewery, pulp and paper, some pharmaceutical streams - at COD typically above 1,500-2,000 mg/L. It suits those duties because it needs no mixing energy and produces a granular sludge that can be sold or reused. It is a poor choice for dilute cold municipal sewage, for streams with high suspended solids that blanket the bed, and for feedstocks where fats, oils and grease are a large fraction of the COD. It is also a poor choice where the operator has no one to watch volatile fatty acids and alkalinity, because the failure mode is fast.
| Design parameter | Typical value or range | Why it matters |
|---|---|---|
| Upflow velocity | 0.5-1.2 m/h at the top | Holds the granular bed without washing it out |
| Organic loading rate | 5-15 kg COD/m3 per day | Set from treatability data, not from vessel volume |
| Temperature | 35-38 degrees Celsius mesophilic | Governs kinetics and process stability |
| Methane yield | 0.25-0.35 m3 per kg COD removed | Follows treatment performance, not the reverse |
| Limitation to check | Dilute cold sewage, high solids and heavy fats are unsuitable | Choose another process for those duties |
| Parameter | UASB reactor | Stirred CSTR digester |
|---|---|---|
| Hydraulic retention | Hours | 20-40 days |
| Organic loading | 5-15 kg COD/m3 per day | 1-4 kg VS/m3 per day |
| Mixing | None - upflow and gas lift | Mechanical, continuous |
| Solids tolerance | Low - needs soluble feed | High - handles 8-12% total solids |
| Typical feedstock | Industrial effluent | Manure, energy crops, sludge |
| Start-up | Weeks to months for granules | Weeks |
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. UASB reactors are supplied with inlet distribution, three-phase separator and gas collection engineered together with the shell, coating selected for the effluent and the vapour space, and sampling and monitoring points positioned so that the bed can actually be managed.
A UASB is bought as a hydraulic design with a tank around it. If the enquiry only specifies volume, you will receive a vessel and be handed the hydraulic problem at commissioning.
If seeded with granular sludge from an operating plant, a reactor can reach design loading in a few weeks. Starting from flocculent sludge, granulation typically takes two to four months, and loading must be increased gradually as the bed develops. Buying or importing seed granules is often the cheapest way to shorten commissioning and should be budgeted at the start.
It can, and it is widely used for that duty in warm climates, but the reactor volume becomes large because the loading rate is limited by temperature and strength, and the effluent usually needs a polishing step. In cooler climates the economics often favour a different process or a heated system. Check the winter temperature before committing.
Hydraulic overloading, which carries the granular bed into the separator and out of the reactor. It is followed closely by fats, oils and grease coating the granules, and by a drop in temperature that reduces activity while loading stays the same. All three are visible in trends before they become failures if someone is watching.
Yes. Reactor height and upflow velocity, inlet distribution design, three-phase separator geometry, gas collection and safety provisions, coating for the effluent and vapour space, sampling points, and heating or insulation are all configured to the wastewater characteristics and the site climate.