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Sunniva Heatpumps
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      • Products
      • Blog
      • Founder's Desk
      • Contact us
      • Calculators
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    Industrial process heat

    How big a heat pump for your process?

    Tell it the shape of the duty and it sizes the machine, prices the heat against what you burn today, and says plainly where the range stops.

    What is it for

    Pick an application, or enter your own duty.

    Pick the closest one and the calculator changes to match it. Choose no application and you enter the duty yourself — which is the right route for anything not on this list.

    The shape of the duty

    Batch, continuous flow, or holding a temperature.

    Flow to heat 2000litres/hour
    Open liquid surface 4m²
    Length × width of the surface. This drives evaporation, which is normally the biggest loss on an open tank.
    Make-up water 100litres/hour
    Cold water added to replace what leaves — drag-out, evaporation, sampling.

    The line

    How many tanks carry heat, and how big they are.

    Tanks that carry heat 3
    Volume of each heated tank 2500litres
    Open surface of each tank 3.5m²
    Length × width of the liquid surface. This is what drives the evaporation, and evaporation is usually the biggest loss on a line.
    Drag-out make-up 60litres/hour
    Solution carried out on the work and replaced with cold water.

    The CIP set

    Tank, make-up per cycle, and the warm return.

    Fresh water per cycle 1500litres
    What is made up from mains each cycle, rather than recirculated.
    Temperature the return comes back at 55°C
    In a pharma plant this stream is clean enough for a plate exchanger to recover from well.
    Tank surface area 22m²
    Shell and top of the hot tank, for the standing loss.

    The vessel and its jacket

    Batch, time, jacket water, and the tank itself.

    Jacket water temperature 80°C
    The single most powerful number here. It sits inside a logarithm, so a few degrees buys far more than a bigger jacket does.
    Temperature drop across the jacket 5°C
    The vessel
    Internal diameter 1.8m
    Liquid height 2.0m
    How far up the shell the batch reaches — only the wetted shell transfers heat.
    Overall heat transfer coefficient 600W/m²K
    Unagitated 150–250; anchor or paddle 400–700; turbine 600–1000; half-pipe coil jacket with good agitation up to 1200.
    Water returning to the heat pump 25°C
    What comes back from the jacket loop for the heat pump to lift again.

    The batch

    Machine type, bath size and how many run together.

    The machine type sets a starting liquor ratio. Airflow machines use the least water; a winch the most.
    Dry fabric per batch 200kg
    Liquor ratio, 1 : 8litres/kg
    Set the bath volume in the Volume slider above.
    Dwell at temperature 60minutes
    Standing loss while holding 3%/hour
    As a share of the heat-up energy, per hour of dwell.
    Vessels in the plant 4
    How many ramp at the same time 2
    This is what sizes the machine. Staggering the schedule is the cheapest capacity you will ever buy.

    The schedule

    How fast, how often, and for how long.

    Time allowed 60minutes
    On a batch duty this is the single biggest lever on machine size: half the time, double the kilowatts.
    Times a day 3
    Hours a day 9hours

    Temperatures

    The rise is what costs money, not the outlet on its own.

    Volume 2000litres
    Temperature the process needs 70°C
    Incoming water temperature 25°C
    What is being heated
    Every degree of process temperature costs money. Across the SE-HT range COP falls from about 4.1 at 60 °C to about 2.7 at 80 °C — a third of the running cost, for twenty degrees many processes do not actually need. If the process will accept a lower temperature, that is the cheapest change available.
    Hours the pre-heater may run 20hours
    Above 80 °C the process draws from an 80 °C tank, so the heat pump refills that tank across the day instead of chasing the peak. More hours means a smaller machine.

    The tanks and the shop floor

    Open surface is where the heat goes.

    What is on the surface
    Tank insulation
    Shell area per tank 11m²
    Shop floor air temperature 32°C
    Relative humidity 60%
    Drier air evaporates more. A humid monsoon shop floor loses less than a dry winter one at the same temperature.

    Heat from the warm stream

    Usually the largest saving available.

    Recover heat from the warm stream
    Most industrial plants throw away a hot stream — spent liquor, CIP return, condensate, effluent. Recovering it makes the heat pump smaller as well as cheaper to run, because it cuts the rise at the cold end where the machine is most efficient.
    Share of the stream that reaches the recuperator 80%
    Temperature lost before it arrives 5°C
    Recuperator effectiveness 55%
    The share of the maximum possible approach the exchanger achieves. Clean condensate reaches 70–85 %; dirty process streams are realistically 50–60 % and need cleaning often.
    Standby machine
    Process heat that stops costs a shift, not a shower. A standby is one spare machine of the same model, piped in parallel and rotated with the duty units.
    Most machines you would accept 4
    Two smaller machines usually fit a process duty far more closely than one large one, and they let you run at part load between batches.
    Sizing margin 10%
    Headroom for fouling, pipe losses and a heavier day than the one you have described.

    What you pay for energy

    Change these to your own rates.

    What makes your process heat today
    The saving is measured against this one doing the whole duty.
    Electricity 9₹/kWh
    Diesel 92₹/litre
    LPG (commercial) 95₹/kg
    PNG 55₹/SCM
    Coal / biomass 9.5₹/kg
    Working days per year 300days
    Comparison assumptions change only if you know why
    Diesel boiler efficiency 80%
    Diesel energy content 10kWh/litre
    LPG boiler efficiency 88%
    LPG energy content 12.8kWh/kg
    PNG boiler efficiency 88%
    PNG energy content 10.5kWh/SCM
    Coal / biomass boiler efficiency 65%
    Coal / biomass energy content 4.5kWh/kg
    Electric heater efficiency 98%
    Whatever figure you have — ours or anyone else’s, installed. Nothing is sent anywhere until you fill in the form below.
    Grid electricity carbon 0.71kg CO₂/kWh
    The Indian grid average. Lower it if you have rooftop solar or a green tariff.
    Diesel carbon 2.68kg CO₂/litre
    LPG carbon 2.98kg CO₂/kg
    PNG carbon 1.9kg CO₂/SCM
    Coal / biomass carbon 1.8kg CO₂/kg
    Swings hugely with grade. Set it near zero for biomass, which is usually counted as biogenic.
    Required heat pump capacity
    —
    The machines that cover it
    —

    Or take it all the way — without the boiler

    What would feed the evaporator?
    Site design air temperature 25°C
    The air temperature the machine has to work in. Both air-source high-temperature ranges publish capacity against this, not against the water temperature.
    Temperature of the water feeding the evaporator 60°C
    The warm stream you are giving up. The R245fa window starts at 22 °C evaporating, so this cannot go much below 27 °C leaving the machine.

    Where the holding load goes

    What the process temperature costs you

    Cost to run for one day

    You would save
    —

    What it pays back, and what it stops

    Pays for itself in
    —
    Carbon avoided
    —

    Want this sizing checked by an engineer?

    Your name, phone and email go on the saved sheet and let our team confirm the duty, the recovery design and the pipe sizing against your actual plant. All three are needed before the sheet can be sent or saved.

    Print / save as PDF

    How this is worked out

    • Every application here is one of three duty shapes — a batch to heat inside a time, a stream to raise continuously, or a temperature to hold against losses. That is why one calculator can cover a plating line and a dyehouse without pretending they are the same thing: the words change, the physics does not.
    • Sensible heat = litres × density × specific heat × temperature rise ÷ 3600. A batch duty is a rate: the same volume in half the time needs twice the kilowatts.
    • A jacketed vessel is not sized on energy over time. The driving difference shrinks as the batch warms, so the correct result is UA = (M·cp ÷ t) × ln((Tj−T1)/(Tj−T2)). Two things follow that a kilowatt figure hides completely: as the jacket water approaches the target the logarithm runs away and no area is enough; and raising the jacket water buys far more than enlarging the jacket, because temperature acts inside the logarithm and area does not.
    • Open tanks lose most of their heat as evaporation, not through the shell. The model is the one validated in our swimming pool calculator: evaporation from the coefficient 25 + 19v kg/m²h against the humidity difference, convection at (3.1 + 4.1v) W/m²K, radiation at emissivity 0.95. It is why floating balls or a lid change a plating line's bill so much.
    • Recovery is worth more than it looks. It cuts the rise at the cold end, where the machine is most efficient, so it shrinks the duty and improves the COP at the same time.
    • The SE-HT range is published at 20 °C ambient, with the outlet temperature varying — 60, 70 and 80 °C. So this calculator interpolates on process temperature, and the figures assume a 20 °C plant room. Cold outside air will reduce output; that correction is not in the published data, so it is not guessed at here. Ask us for the ambient correction on a specific site.
    • Process temperature is the biggest lever on the bill. Across the SE-HT range COP falls from about 4.1 at 60 °C to about 2.7 at 80 °C — a third of the running cost. If the process will accept less, that is the cheapest change available.
    • Above 80 °C the SE-HT range stops, and you get two answers instead of one. The first re-sizes the SE-HT as a pre-heater feeding a tank, with your existing boiler taking the last stretch — usually most of the energy moved off fuel, for the easiest retrofit there is. The second sizes a machine that takes the whole lift and removes the boiler altogether, against the same duty, so the two can be compared on one screen.
    • The high-temperature ranges are selected on the SOURCE, not on the water. SE-HT publishes capacity against outlet temperature at a fixed 20 °C plant room. None of the three ranges above it does: SE-SHT and the SE-UHT cascade both publish against ambient air at a fixed outlet, so the section asks for a site design temperature; the single-cycle SE-WWUHT publishes one rated point, at 60 / 55 °C into the evaporator, so it is selected on duty at that condition and nowhere else. There is no source-temperature curve for it, and this page does not invent one.
    • The single cycle has a hard floor, not a derating. Its R245fa compressor window starts at 22 °C evaporating. Feed the evaporator below roughly 27 °C and the machine is outside its permitted envelope entirely — so the page withdraws the selection rather than quoting a reduced one, and sends you to the cascade, which needs nothing warm from the site.
    • Defaults are indicative starting figures for each application, not Sunniva product data. They are all sliders, and the saved sheet records exactly what was used.
    • Payback is simple payback — the price you type in, divided by the annual saving. No finance, no maintenance, no discounting, and no price of ours is assumed or disclosed. Carbon is the displaced fuel’s emissions minus the electricity the heat pump draws, at the Indian grid average of 0.71 kg CO₂ per unit. Every factor is a slider, and the saved sheet records what was used.
    • Indicative only. Process detail, schedule, pipe runs and water quality all affect the final design — confirm with Sunniva Encon LLP before ordering.
    Industrial process heat sizing Sunniva Encon LLP

    Calculated for

    —

    What you entered

    Result

    Required capacity
    —
    —

    Running cost & savings

    How this was worked out

    Talk to Sunniva

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    Contact
    +91 93213 65103
    sales@sunnivaencon.com
    www.sunnivaencon.com
    Office
    C‑443, Oshiwara Industrial Centre Premises CHS, New Link Road, Goregaon West, Mumbai
    © 2026 Sunniva Encon LLP. The design and code of this calculator are our copyright. Results are indicative and offered in good faith — the method is set out above. Confirm the final selection with us before ordering.
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    At Sunniva Encon, we specialize in manufacturing high-quality heat pumps designed to meet the unique needs of the Indian market. Since 2012, we've been committed to providing sustainable and efficient heating and cooling solutions.

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