Estimate a mining site in two linked balances: first calculate the electrical demand of the exact miners and every in-boundary auxiliary system; then treat almost all of that electricity as heat that must be moved outside the same boundary. A credible first pass therefore requires an equipment inventory, an explicit facility boundary, a simultaneous-load calculation, a heat conversion, and a cooling design checked against local weather, water, airflow, and equipment limits.
The result is a planning estimate, not construction-ready electrical or mechanical engineering. Final sizing requires current equipment documentation, utility data, local design weather, applicable codes, and qualified engineers.
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What the estimate must answer
A mining-site estimate should answer four separate questions rather than produce one unexplained number:
- How many kilowatts will the miners draw at the operating settings you intend to use?
- How much additional demand belongs to cooling, pumps, fans, controls, networking, lighting, and other equipment inside the selected boundary?
- How much heat will that boundary generate during normal and maximum simultaneous operation?
- Can the proposed cooling path reject that heat under the site’s worst relevant ambient, water, electrical, and maintenance conditions?
Keep three electrical measures distinct. Demand is the instantaneous or interval load the utility and distribution system must support. Energy is demand accumulated over time, expressed in kilowatt-hours. Capacity is the rating of the service, transformer, switchgear, cooling plant, or container that limits how much equipment can operate. A site can have enough annual energy available yet lack the instantaneous capacity to run its miners on a hot afternoon.
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Step 1: Build an exact miner inventory
Start with one row for every miner model and operating mode. Do not estimate from hashrate, joules per terahash, or a model example when the actual wall-power specification is available. Hashrate describes computing output; the electrical service must be sized from watts.
Fields to record for each row
- Manufacturer and exact model or board revision.
- Quantity that can run simultaneously.
- Specified wall power at the intended firmware, frequency, voltage, and inlet condition.
- Input voltage, phase, frequency, connector, and allowable tolerance.
- Airflow direction and required flow, or liquid flow, pressure, coolant, and supply/return temperatures.
- Permitted inlet-temperature and humidity range.
- Specification revision or publication date and the source used.
Then calculate each row as:
Miner load (kW) = quantity × specified wall power (W) ÷ 1,000.
Sum the rows only after deciding whether the quantities represent normal operation, a maximum simultaneous case, or a deliberately throttled mode. If a miner has a documented operating range, calculate at least the expected setting and the highest setting that could be enabled by the operator or firmware.
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ViaBTC’s September 11, 2026 article reproduces manufacturer figures for a Bitmain Antminer S21 XP: typical wall power of 3,645 W at 25°C inlet air, typical hashrate of 270 TH/s, and 220–277 V AC single-phase input. The article also reports manufacturer tolerances around the typical values. For planning, the relevant starting number is 3.645 kW per unit, not the 270 TH/s hashrate.
If a proposed row contained 100 units at that stated typical power, the miner-only demand would be 364.5 kW. That arithmetic is an illustration using the published model figure; it is not a current specification for every S21 XP revision or a substitute for the procurement document for your units.
Step 2: Draw the facility boundary before adding anything
State exactly what the estimate includes. Common boundaries are:
- Miner-only: ASIC wall power, useful for a quick equipment inventory but inadequate for utility or cooling design.
- Container or room: miners plus fans, pumps, controls, networking, lighting, and cooling equipment located in that container or room.
- Whole site: all mining halls, cooling plant, water treatment, offices, workshops, security, distribution losses, and other loads supplied by the service.
List every load inside the chosen boundary. Typical auxiliaries include supply and exhaust fans, evaporative pads or spray pumps, dry coolers, chillers, cooling towers, liquid pumps, heat exchangers, controls, sensors, network switches, lighting, water-treatment equipment, and trace heating. Add transformers or distribution losses only when they are within the boundary you are trying to balance.
Avoid double-counting vendor ratings
Read the scope of every continuous-power or container rating. Some vendors quote a rating that already includes ancillary equipment. Upstream Data’s 200 kW Hash Hut specification, for example, says its continuous rating is based on a maximum 4,000 W per miner while including ancillary loads. Its sheet lists a maximum cooling ancillary load of 7.5 kW and networking, control, and lighting of 0.5 kW. Those are product-specific figures, not universal allowances.
For a rating that includes auxiliaries, the relationship is:
Available ASIC capacity = (continuous facility rating − included ancillary load) ÷ ASIC load rating.
Use the formula only after confirming that the rating, ancillary figures, and ASIC load are stated on the same basis. Do not add the 7.5 kW and 0.5 kW again if they are already included in the 200 kW rating. Conversely, do not subtract them if the quoted rating is explicitly miner-only.
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Keep demand and energy in separate worksheets
For a steady load, energy (kWh) = demand (kW) × operating hours. A 3.645 kW miner operating continuously for 24 hours uses 3.645 × 24 = 87.48 kWh per day, matching the worked arithmetic published by ViaBTC. The figure is an arithmetic example based on the stated typical wall power, not a field measurement.
Track at least:
- Normal average demand.
- Maximum simultaneous demand, including all miners and auxiliaries that can run together.
- Startup or transient demand where motors, pumps, or compressors may begin together.
- Daily, monthly, and annual energy under the operating schedule.
Do not insert an arbitrary “safety percentage” and present it as engineering reserve. Any reserve should be an explicit decision by the electrical designer, utility, equipment vendor, or applicable code.
Step 3: Convert the electrical load into heat
Within a room, container, or building boundary, nearly all electricity consumed by computing equipment eventually becomes heat. BITMAIN’s computer-center guidance states that about 98% of electrical consumption changes into heat energy. For a first-pass mining balance, the numerical heat load in kilowatts is therefore approximately equal to the in-boundary electrical load in kilowatts.
When a cooling calculation uses imperial units, ViaBTC gives the standard conversion as 1 W = 3.412 Btu/h, or approximately 1 kW = 3,412 Btu/h. Its S21 XP example multiplies 3,645 W by 3.412 to obtain approximately 12,437 Btu/h per miner. Treat that as a model-specific arithmetic illustration, not a universal miner rating.
What belongs in the heat balance
Include the heat from miners and every in-boundary auxiliary electrical load. Fans, pumps, controls, networking equipment, lighting, and power-conversion losses all add heat. Cooling equipment requires special care: its electrical input becomes heat somewhere, but not necessarily on the same side of the heat exchanger. A chiller located inside the room adds its compressor and fan heat indoors while rejecting the removed miner heat outdoors. A remote dry cooler may place most of its electrical heat outdoors. State the thermal boundary and the location of each component before adding loads.
BITMAIN Support advises that equipment heat dissipation should be based on the equipment’s actual power consumption. ASHRAE Chapter 20 similarly states: “The goal of a good datacom facility cooling design is to match cooling capacity to actual heat load.” These principles rule out selecting cooling capacity from a generic number of miners without checking their actual operating power.
Step 4: Size the cooling path rather than just its nameplate
A cooling nameplate is only useful if the complete path can move heat from the miner inlet to the final outdoor heat sink under design conditions. Trace that path: miner, room or liquid loop, heat exchanger, fan or pump, outdoor rejection equipment, controls, and exhaust or water-disposal route.
Air cooling calculation
Air systems carry sensible heat away through a temperature rise. A first-pass relationship is:
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Use air density for the site’s altitude and operating temperature, and use the allowable rise between the selected inlet and exhaust points. The equation shows the trade-off: a larger heat load requires more airflow, while permitting a larger temperature rise reduces the required flow. Neither result is a fan selection by itself.
Check the selected fan at the actual static pressure, not its free-air rating. Include louvers, filters, ducts, screens, acoustic treatment, weather hoods, and fouling. Verify the fan curve at the operating point and confirm that redundant equipment can maintain the required flow if one unit is unavailable.
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Protect miner inlets from recirculation
Separate hot exhaust from cool intake air. Short-circuiting exhaust back to miner inlets raises inlet temperature even when the fan’s nominal airflow appears adequate. ASHRAE describes inlet temperature, upstream air heating, and equipment self-heating as interacting factors. Layout, pressure balance, blanking panels, duct seals, and weather openings can matter as much as fan capacity.
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Evaluate the hottest relevant outdoor design condition, not the annual average. Include humidity, solar exposure, dust, wildfire smoke, rain, and condensation risk where applicable. BITMAIN recommends climate-aware air distribution, filtration, airflow balance, and avoiding dew or condensation. The miner’s allowable inlet envelope remains the controlling limit.
Liquid and container cooling
Liquid systems must be sized from the equipment supplier’s specified flow, pressure, coolant, supply temperature, return temperature, heat exchanger approach, and outdoor heat-rejection condition. A pump that meets a catalog flow at zero pressure may fail once piping, filters, valves, heat exchangers, and elevation are included.
BITMAIN’s AntSpace HK3 V2 parameter sheet provides a useful example of the fields that must be collected. For that version, it describes 210 miners, up to 1,100 kW total consumption, 52 kW supporting consumption, 1,000 kW heat dissipation, 230 m³/h spray-pump flow, and external spray-water consumption of 1.15 m³/h. It gives 35°C miner inlet water and 45°C outlet water. BITMAIN warns that another manufacturer or version may differ. These figures demonstrate the data to request; they are not a sizing rule for another container.
For immersion or liquid-cooled equipment, verify compatibility of the miner, dielectric or water-based fluid, seals, hoses, manifolds, heat exchangers, pumps, controls, and service procedures. Confirm how leaks are detected and contained, how fluid quality is maintained, and whether the heat rejection remains within limits during the hottest weather or a partially failed system.
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No single architecture is universally best. Compare the complete operating envelope, not only the purchase nameplate.
| Design axis | Air or evaporative-assisted | Water-cooled or immersion |
|---|---|---|
| Climate | Ambient temperature and humidity determine how much cooling is available and increase the risk of hot-air recirculation on hot days. | Ambient conditions affect dry or wet heat rejection and may constrain practical supply and return temperatures. |
| Water | Evaporative pads, mist, or sprays consume water; quantify the local rate, quality, storage, treatment, and disposal requirements. | Closed loops still may use water at cooling towers or spray heat rejection. Check the exact design rather than assuming zero consumption. |
| Auxiliary power | Fans, controls, filters, and evaporative equipment add electrical demand. | Pumps, dry coolers, cooling towers, heat exchangers, and chillers add electrical demand. |
| Equipment compatibility | Confirm airflow direction, inlet temperature, filtration, and humidity limits for every miner. | Confirm container or miner compatibility, coolant, flow, pressure, temperature, fluid quality, and leak-control requirements. |
| Operations | Plan filter replacement, dust control, weather protection, airflow balancing, noise management, and hot-air separation. | Plan pump and heat-exchanger maintenance, fluid testing, leak detection, controls, spares, and safe draining or isolation. |
| Heat recovery | Exhaust air is commonly lower-temperature heat; determine whether it is useful for the intended load. | Some liquid arrangements can deliver warmer heat, depending on operating temperatures and heat-exchanger design. |
A U.S. Department of Energy report modeling 30 MW Texas crypto-mining data-center scenarios includes outside-air cooling with evaporative pad or mist assistance and no chillers, immersion cooling with hybrid dry or wet heat rejection, and dry-cooler/liquid-loop alternatives. The scenarios show that several architectures can be modeled; they do not establish an optimum for a different site.
Step 6: Check electrical and thermal constraints together
Cooling consumes part of the same electrical capacity needed by the miners. If the utility or transformer can deliver 1,000 kW to a site, the miner allocation is lower than 1,000 kW whenever fans, pumps, chillers, controls, and other in-boundary equipment are operating.
Use a simultaneous-load schedule
- List every miner row and mark whether it runs in the normal, maximum, or reduced-power case.
- List every auxiliary device and identify its normal, maximum, and standby demand.
- Mark which devices can run simultaneously, which start sequentially, and which are redundant.
- Calculate miner demand, auxiliary demand, total demand, and energy separately.
- Repeat the calculation for the hottest design condition, a failed cooling component, and any planned expansion.
Then compare the resulting demand with the utility service, transformers, switchgear, distribution equipment, and cooling plant ratings. Voltage, phase, conductor, protective-device, grounding, arc-flash, and code decisions require a qualified electrical engineer; the inventory does not establish a breaker size or service rating.
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An average load can conceal a thermal failure. A site may run comfortably overnight and exceed miner inlet limits during a hot afternoon, after filters foul, or when an evaporative system runs short of treated water. Record the design ambient, maximum inlet temperature, permitted humidity, water temperature, flow, and pressure alongside every capacity figure.
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The estimate becomes useful only when measurements can confirm its assumptions. Install metering and sensors at the boundary used in the calculation.
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Electrical measurements
- Per-panel or per-container voltage, current, power factor where relevant, real power in kW, and accumulated kWh.
- Separate miner and auxiliary circuits so an apparent reduction in miner load is not confused with a cooling increase.
- Maximum simultaneous demand and alarm thresholds below the equipment or service limit.
- Phase balance and abnormal voltage conditions within the equipment’s specified input range.
Air-system measurements
- Miner inlet temperature and humidity at representative locations, including the hottest row.
- Outdoor temperature and humidity, supply and exhaust temperatures, and evidence of exhaust recirculation.
- Fan speed, airflow or differential pressure, filter pressure drop, and damper position.
- Condensation or dew-risk alarms where humid outdoor air can contact cold surfaces.
Liquid-system measurements
- Supply and return temperature, flow, pressure, pump status, and heat-exchanger approach temperature.
- Fluid quality, level, leak detection, and water-treatment status where applicable.
- Outdoor heat-rejection temperature, fan or spray-pump status, and water consumption.
- Alarm history tied to miner throttling or shutdown.
Commission at partial load and then at the highest safe simultaneous load. Compare measured electrical demand and temperatures with the worksheet, investigate deviations, and update the operating limits. A measurement program cannot replace design engineering, but it can expose double-counted auxiliaries, blocked airflow, incorrect sensor placement, or an optimistic vendor assumption before the fleet is fully deployed.
Common estimation mistakes and corrections
Using hashrate as a power rating
Hashrate does not tell the service how many watts the miner will draw. Correct the worksheet with the exact wall-power specification for the firmware and operating mode.
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Adding every vendor number together
A facility rating may already include cooling, networking, controls, and lighting. Read the rating scope and subtract or separate included loads before adding them.
Cooling only the miner nameplate
Fans, pumps, lighting, networking, and other in-boundary electrical loads also become heat. Recalculate the thermal balance from the complete boundary.
Selecting fans from free-air airflow
Filters, ducts, louvers, screens, and fouling create static pressure. Select from the fan curve at the real pressure and verify the hottest operating case.
Assuming a closed liquid loop uses no water
Heat rejection may still use spray or cooling-tower water. Obtain the specified consumption, treatment, storage, and discharge requirements.
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Generalizing a container’s published figures
The AntSpace HK3 V2 and 200 kW Hash Hut values apply to those stated products and configurations. They do not establish a universal support-load percentage, miner count, water rate, or heat-dissipation figure.
A reusable planning worksheet
Set up one sheet with the following columns:
- Model, revision, operating mode, quantity, and specification date.
- Wall watts per unit and calculated miner kW.
- Input voltage and phase, airflow or liquid requirements, and allowable inlet conditions.
- Auxiliary equipment, quantity, normal kW, maximum kW, and whether its load is already included in a vendor rating.
- Boundary location for each load and whether its heat is indoors, outdoors, or transferred through a heat exchanger.
- Total normal demand, maximum simultaneous demand, heat in kW, and heat in Btu/h if required.
- Design ambient, permitted temperature rise, calculated airflow or liquid flow, and the selected equipment’s operating point.
- Measurement point, alarm limit, responsible operator, and commissioning result.
Attach the actual specification sheets and record any assumptions beside the number they affect. When a value is unavailable, mark it as not stated and obtain it before treating the estimate as a capacity decision.
What this first-pass method cannot establish
The available figures do not establish a universal power-usage effectiveness value, airflow-per-miner number, facility reserve margin, service size, breaker rating, cooling-tonnage requirement, annual operating cost, or annual water requirement. Those values depend on the exact fleet, architecture, local weather, utility arrangement, codes, controls, and operating policy.
Use the worksheet to identify the required capacity and missing information. Proceed to detailed electrical and mechanical design only after the equipment schedule, boundary, weather data, water conditions, utility capacity, redundancy objectives, and code requirements have been reviewed by qualified professionals.
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