logo.png

sales@cectank.com

86-020-34061629

English

Data Center Thermal Energy Storage Tanks: How Cold Storage Improves Cooling Efficiency

Created on Today
Data Center Thermal Energy Storage Tank
Data Center Thermal Energy Storage Tanks: How Cold Storage Improves Cooling Efficiency
A data center thermal energy storage tank holds chilled water produced during off-peak hours and discharges it during the peak, so chillers run at a steady, efficient load instead of tracking hourly IT heat. With a usable temperature difference of 4-7 K and a realistic usable fraction of 70-90%, one stratified tank carries several hours of cooling load and gives operators a defined ride-through window when chillers trip. The tank does not create cooling; it moves that cooling in time.
In a hyperscale hall the IT load curve is fairly flat while the cooling plant is sized for a hotter design day, yet measured load spends most hours far below that ceiling, so the plant runs at low part-load and still absorbs every fast heat spike the racks deliver.
Many tariffs charge for peak demand in kW as well as energy in kWh, so a plant chasing every IT spike pays for the spike rather than for the kilowatt-hours consumed. When a chiller trips, the only thing between a rising return temperature and a shutdown is the water still sitting in the pipes.
A data center thermal energy storage tank addresses both by relocating cooling in time instead of generating more of it during the peak. What follows covers what the vessel is, where it sits in the chain, how to size it, and which operating modes justify the spend.

What a Data Center Thermal Energy Storage Tank Is

An insulated volume of chilled water, held at supply temperature and returned to the plant loop whenever demand exceeds what the chillers are set to deliver. Nothing inside it makes refrigeration.
· Storage, not generation. It holds energy the chillers already paid for, so comparing it with a larger chiller plant compares capital against a demand charge and a part-load penalty.
· Charged at the plant's efficient point. In the off-peak window chillers run near full load and make water at 4-6 °C while the volume fills, so the chiller never follows the afternoon IT curve.
· Discharged inside the same band. Supply leaving the tank normally sits at 6-8 °C, so blending with the chiller stream never pushes the loop above the temperature IT equipment accepts.
· A finite duration, not autonomy. A tank sized for four peak hours provides four hours under the assumed load, and stating that duration is the first step of any credible thermal energy storage tank data center study.

Where the Tank Sits in the Cooling Chain

A thermal energy storage tank for data centers is commonly connected on the common pipe between the chiller plant and the distribution header, in parallel with the chillers rather than behind them. That arrangement fixes the control logic, the valve inventory and plant behaviour at handover.
· Chiller loop and distribution loop. Each feeds the common pipe through isolation and check valves, and a distribution-side pump set draws from whichever combination the control has selected, keeping the tank independent of evaporator pressure. Storage may also sit upstream of the chillers, blending discharge with return before the evaporators at the cost of full system flow through the tank.
· Handover, bypass, fill and drain. Logic should change the chiller setpoint before the isolation valve opens, so supply temperature neither dips nor recovers. The plant also needs a service bypass, a fill and vent path, and a drain, because a tank that cannot be emptied cannot be inspected.

Sizing: From IT Load to Tank Volume

Volume is not a judgement call; it follows from the load, the temperature difference and the hours covered.
1. Find the duty and flow. Divide the IT heat load assigned to storage by the loop ΔT. A 5 MW hall at 7 K needs roughly 615 m³/h.
2. Apply the energy equation. Q = V × ρ × cp × ΔT, with water at cp ≈ 4.186 kJ/kg·K and ρ ≈ 1000 kg/m³, about 1.163 kWh per cubic metre per kelvin, so roughly 7 kWh theoretical per m³ at a 6 K usable ΔT.
3. Apply the usable fraction. Mixing, ambient gain and short-circuiting remove part of the theoretical value; designers count on 70-90%, the lower figure for a tall shell with a poorly placed diffuser.
4. Convert to a vessel. Divide usable energy by duty and hours, then round to a practical diameter and shell height.

Operating Modes That Justify the Tank

Full storage charges off-peak and shuts the plant during the peak, giving the largest demand saving and the largest volume: a full tank at start of day, empty at finish. Ride-through carries the Tier III or Tier IV case, where a chiller taken for maintenance would otherwise be unplanned.

Technical Specification

Interface items generate most of the engineering change on a storage project.
Item
Typical value or choice
Drives
Vessel boundary
Atmospheric field-erected, or inside the system pressure boundary
Shell thickness, nozzle ratings, relief
Usable ΔT
4-7 K, commonly 6 K (5 °C to 11 °C)
Stored energy per cubic metre
Charge and discharge temperature
4-6 °C charging, 6-8 °C discharge
IT inlet band and blending margin
Usable fraction
70-90% of theoretical
Gross volume
Inlet velocity
0.5-1 m/s through the diffuser
Stratification quality
Nozzle and instrument list
Charge, discharge, return, fill, vent, drain, level, manway
Valve count and access
Insulation
Mineral wool, weather barrier, continuous cladding
Standing heat gain
Foundation
Ring beam or pad with thermal bridge detail at supports
Shell registration and freezing detail

Project Case

Our delivered reference work in the water and wastewater sector includes large-diameter bolted tanks erected on site, such as the four-shell installation below, and the data-center TES scope is engineered to the same standards.

Project Case Summary

Project
Product
Capacity
Dimensions
Completion
Namibia - drinking water storage (P-A)
01 GFS bolted glass-fused-to-steel tank
44,900 m³ total, 4 tanks
4 × φ41,260 mm × 8,400 mm
September 2022
Those shells left the factory as enamel-coated panels, shipped as discrete courses and built ring by ring on site. That erection sequence and holiday test are what the cooling-side vessel inherits.

Center Enamel Engineering Capability

Center Enamel (Shijiazhuang Zhengzhong Technology Co., Ltd) has designed and fabricated bolted storage tanks since 2008. As the first glass-fused-to-steel (GFS) tank manufacturer in China, the company holds close to 200 enamel-related patents, produces roughly 300,000 enamel-coated steel plates a year, has completed more than 30,000 installed projects and supplies its tanks to over 100 countries. The new 150,000 m² production base was added to raise output capacity, and single tanks are supplied up to 60,000 m³. Manufacturing runs under ISO 9001 and ISO 45001, with product certification including NSF/ANSI 61, WRAS, FDA, LFGB, CE (EN 1090), ISO 28765, FM, BSCI and EUROCODE, and design referenced to AWWA D103-09, AWWA C550 and NFPA where the application requires it.
Storage shell and water quality
· Glass-fused-to-steel shells are enamelled at 820-930 °C with a 0.25-0.45 mm enamel layer, 3450 N/cm² adhesion, a 1500 V DC holiday test and Ra below 0.8 µm, which keeps the internal surface smooth enough to hold a stable thermocline with low parasitic pressure loss.
· Atmospheric bulk chilled-water service is covered by the AWWA D103-09 design route and ISO 28765 factory production control, with NSF/ANSI 61 and WRAS applicable when the water is classified as potable-grade system fluid.
· Our reference record for large-diameter, high-capacity atmospheric water tanks includes the Namibia potable water scheme of 4 × φ41.26 m × 8.4 m tanks totalling 44,900 m³, completed in 2022-09.

Frequently Asked Questions

Q1: Does a data center thermal energy storage tank reduce the number of chillers bought?
A1: Only under full storage. If the plant shuts chillers completely in the peak, it can be sized for average rather than peak load. In partial-storage or ride-through designs the chillers keep their size and the tank covers part of the peak.
Q2: How many hours of storage make economic sense?
A2: Most projects fall between two and six peak hours. Below two a tank competes with a simple buffer vessel and the capital does not separate from the benefit; above roughly six, volume and footprint grow while the saving per cubic metre falls.
Q3: Can the tank sit inside the pressure boundary of the chilled water system?
A3: It can, though an atmospheric field-erected vessel is common for large volumes because wall thickness and nozzle design stay simple and the shell can be inspected from inside. On the pump discharge side it joins the pressure boundary, then thickness, openings and relief are calculated to the design pressure and temperature in the specification.
Q4: What happens when chillers stop and pumps stop with them?
A4: A tall insulated tank loses little heat over a few hours; the real risk is mixing. If warm return water still enters while circulation has stopped, the thermocline migrates upward and usable cold shrinks faster than the heat balance suggests. A full tank holds its charge longer than a partly discharged one.
Q5: Does standing chilled water need special treatment?
A5: Yes. Stagnant chilled water is prone to biological growth and to corrosion of carbon steel attachments when oxygen is present, so biocide, pH control and periodic inspection belong in the commissioning plan, and the lining must suit the treatment programme the plant already runs.
A data center thermal energy storage tank decouples the chiller plant from the instantaneous heat rejection demand of the IT load. Pick the usable temperature difference, apply the energy equation with a realistic usable fraction, and check discharge flow against loop pump capacity. Where demand charges dominate the commercial case is clear; where a chiller outage would otherwise be unplanned, the reliability case carries it.
A tank that meets its usable capacity is separated from one that falls short by detail: inlet velocity, diffuser placement, insulation continuity at the supports, and the control logic at handover.

Talk to an Engineer

Send us the IT load curve, supply and return temperatures, the tariff structure and the plot area. We will work through a tank sizing calculation with you, state the usable fraction we would guarantee for the proposed geometry, and return a specification sheet covering diameter, straight height, nozzle list, insulation thickness and coating selection. Where the chiller order is still open, discuss TES integration before it is placed, because the connection arrangement decides most of the control logic.
WhatsApp