Tell us the job. We will build the machine.
The thirteen published ranges cover most jobs. This page is for the ones they do not — a temperature, a duty, a water quality or an environment that wants a machine designed around it. Work out the duty, choose the build, and our engineers come back with the machine, the price and a delivery time.
The duty
The part we can actually work out for you.
The source, and the water
Where the heat comes from, and what it has to survive.
The build
Cabinet, controls and how the compressors are arranged.
The circuit
Refrigerant, condenser, and anything else it has to do.
What you pay for energy
For the comparison panel. Change these to your own tariff.
Notes for our engineers
The things a form never asks about.
Fuel and efficiency assumptions change only if you know why
This is an enquiry, not a quotation
The kilowatts above are worked out from your own figures and hold for any machine. Everything below is what you are asking for — there is no data sheet behind a machine that has not been built, so this page quotes no capacity, no COP and no price for it. Send it and our engineering team comes back with all three.
What follows from the duty
Your configuration
What our engineers will look at
Cost to run for one day
Send this to our engineering team
Your name, phone and email go on the sheet and let our team come back with the machine, the price and a delivery time. All three are needed before the enquiry can be sent or saved.
How this page works, and where it stops
- The duty is computed. The machine is not. Kilowatts from flow × density × specific heat × temperature rise, or from a batch over the time you allow. That arithmetic is true of any heat pump ever built, so it does not need a data sheet. The configuration below it is recorded, and deliberately carries no capacity or COP — those come out of the engineering review, not out of a web form.
- Why there is no price. A custom machine is priced from its bill of materials, and that does not exist until it has been designed. Any number this page produced would be wrong, and you would quite reasonably hold us to it.
- The COP in the cost panel is yours, not ours. The comparison needs some figure to work from, so the slider is there and labelled. It is a way of asking “what would this be worth if it ran at 3.0?”, not a rating.
- Refrigerant against delivery temperature is checked against the published compressor envelopes we actually build on — the same windows behind the High, Super High and Ultra High Temperature pages. R410A to about 60 °C, R134a and R1234ze to 80, R515B to 95, R245fa and the cascade to 120.
- R245fa needs a warm source, and that is physics. Its compressor window starts at 22 °C evaporating. Fed with ambient air it is outside its permitted envelope entirely — not derated, outside it. Where you want 120 °C from air, the cascade is the answer.
- Water quality picks the condenser. Chloride wants titanium; nothing else survives a pool or brackish water. Acidic or deionised water attacks the copper braze in a standard plate exchanger, so it wants the stainless-brazed one. Water carrying solids wants a tube in shell, because that is the one you can actually rod.
- Buffer volume of 12 to 25 litres per kilowatt keeps the compressor off a short cycle and gives a defrost somewhere to draw from. Pipe size is set at a 1.5 m/s velocity ceiling. Both are rules of thumb, and both are on the sheet so you can see what was assumed.
- Everything you enter is recorded on the saved sheet, including the assumptions. Confirm the final design with Sunniva Encon LLP before ordering.
Calculated for
What you entered
Result
Running cost & savings
How this was worked out
Talk to Sunniva
Contact
+91 93213 65103sales@sunnivaencon.com
www.sunnivaencon.com
Office
C‑443, Oshiwara Industrial Centre Premises CHS, New Link Road, Goregaon West, MumbaiTell us the job. We will build the machine.
The thirteen published ranges cover most jobs. This page is for the ones they do not — a temperature, a duty, a water quality or an environment that wants a machine designed around it. Work out the duty, choose the build, and our engineers come back with the machine, the price and a delivery time.
The duty
The part we can actually work out for you.
The source, and the water
Where the heat comes from, and what it has to survive.
The build
Cabinet, controls and how the compressors are arranged.
The circuit
Refrigerant, condenser, and anything else it has to do.
What you pay for energy
For the comparison panel. Change these to your own tariff.
Notes for our engineers
The things a form never asks about.
Fuel and efficiency assumptions change only if you know why
This is an enquiry, not a quotation
The kilowatts above are worked out from your own figures and hold for any machine. Everything below is what you are asking for — there is no data sheet behind a machine that has not been built, so this page quotes no capacity, no COP and no price for it. Send it and our engineering team comes back with all three.
What follows from the duty
Your configuration
What our engineers will look at
Cost to run for one day
Send this to our engineering team
Your name, phone and email go on the sheet and let our team come back with the machine, the price and a delivery time. All three are needed before the enquiry can be sent or saved.
How this page works, and where it stops
- The duty is computed. The machine is not. Kilowatts from flow × density × specific heat × temperature rise, or from a batch over the time you allow. That arithmetic is true of any heat pump ever built, so it does not need a data sheet. The configuration below it is recorded, and deliberately carries no capacity or COP — those come out of the engineering review, not out of a web form.
- Why there is no price. A custom machine is priced from its bill of materials, and that does not exist until it has been designed. Any number this page produced would be wrong, and you would quite reasonably hold us to it.
- The COP in the cost panel is yours, not ours. The comparison needs some figure to work from, so the slider is there and labelled. It is a way of asking “what would this be worth if it ran at 3.0?”, not a rating.
- Refrigerant against delivery temperature is checked against the published compressor envelopes we actually build on — the same windows behind the High, Super High and Ultra High Temperature pages. R410A to about 60 °C, R134a and R1234ze to 80, R515B to 95, R245fa and the cascade to 120.
- R245fa needs a warm source, and that is physics. Its compressor window starts at 22 °C evaporating. Fed with ambient air it is outside its permitted envelope entirely — not derated, outside it. Where you want 120 °C from air, the cascade is the answer.
- Water quality picks the condenser. Chloride wants titanium; nothing else survives a pool or brackish water. Acidic or deionised water attacks the copper braze in a standard plate exchanger, so it wants the stainless-brazed one. Water carrying solids wants a tube in shell, because that is the one you can actually rod.
- Buffer volume of 12 to 25 litres per kilowatt keeps the compressor off a short cycle and gives a defrost somewhere to draw from. Pipe size is set at a 1.5 m/s velocity ceiling. Both are rules of thumb, and both are on the sheet so you can see what was assumed.
- Everything you enter is recorded on the saved sheet, including the assumptions. Confirm the final design with Sunniva Encon LLP before ordering.
Calculated for
What you entered
Result
Running cost & savings
How this was worked out
Talk to Sunniva
Contact
+91 93213 65103sales@sunnivaencon.com
www.sunnivaencon.com