UASB Tank for Biogas Project: The Reactor, Not the Gas Holder

Product Details
Place of Origin: China
Brand Name: CEC TANKS
Certification: ISO 9001:2008, AWWA D103 , OSHA , BSCI
Model Number: W20161227006
Payment & Shipping Terms
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

Product Description

UASB Tank for Biogas Project: The Reactor, Not the Gas Holder

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.

1. What Is a UASB Reactor?

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.

  • No Mechanical Mixing: Upflow and biogas lift provide contact. Mechanical mixers would shear the granules that make the process work.
  • Granular Biomass: A well-run bed holds 20-40 g/L of volatile suspended solids as settleable granules, which is why the reactor can be small.
  • Three-Phase Separator: Gas, liquid and solids must be separated at the top; this component, not the shell, sets the hydraulic ceiling.
  • Short Retention, High Rate: Hours rather than days, at 5-15 kg COD/m3 per day for suitable effluent.
  • Gas Is a By-Product of Control: Roughly 0.25-0.35 cubic metres of methane per kg of COD removed - so gas yield follows treatment performance, not the other way round.

2. Which Parameters Decide Whether It Works?

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.

  • Upflow Velocity: About 0.5-1.2 m/h at the top of the reactor. It is the single most consequential operating number.
  • Organic Loading Rate: Typically 5-15 kg COD/m3 per day for suitable effluent. Set it from treatability data, not from the vessel volume you happen to have.
  • Temperature: Mesophilic 35-38 degrees Celsius is standard. Stability matters more than the setpoint - swings of several degrees stress the biomass.
  • Alkalinity and pH: Enough buffering to hold pH near 6.8-7.4; volatile fatty acid accumulation is the earliest warning of overload.
  • Inhibitors and FOG: Sulphate, ammonia, disinfectants and fats, oils and grease all change the design. Fats in particular coat granules and cause floating sludge.

3. When Is UASB Right, and When Is It Not?

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.

  • Good Fit: Soluble, warm, readily degradable industrial effluent above roughly 1,500-2,000 mg/L COD.
  • Poor Fit - Dilute and Cold: Low-strength municipal sewage at ambient temperature often cannot sustain the loading the process needs.
  • Poor Fit - High Solids: Suspended solids fill the bed and reduce the active granular fraction; upstream removal is needed first.
  • Poor Fit - Heavy FOG: Fats coat granules, cause floatation and washout, and need pre-treatment rather than a bigger reactor.
  • Operations Matter: VFA, alkalinity and gas composition should be trended. A UASB with no monitoring fails faster than a stirred digester with the same neglect.
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

Engineering Assurance and Project Support

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.

Frequently Asked Questions (FAQ)

How long does it take to start up a UASB reactor?

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.

Can a UASB treat municipal sewage?

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.

What is the most common cause of UASB failure?

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.

Can the UASB tank be customized to our wastewater?

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.

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Shijiazhuang Zhengzhong Technology Co., Ltd
sales@cectank.com
86-20-34061629
Fuli Commercial Center room 301#, Xingang West Rd.11#, Haizhu area, Guangzhou, Guangdong province, China.
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