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Sunniva Encon LLP · Application NoteAN-024 · Rev 0 · 23 Oct 2026
Dairy and food processing

Coffee extraction water heated with evaporator heat

How a soluble coffee plant extracting 3 tonnes of roast coffee a day can heat its extraction water with a heat pump fed from its extract evaporator, cutting furnace-oil boiler steam.

Application#24 Extracting instant coffee and tea
Temperature band90–110 °C
Sunniva selection4 × SE-WWUHT-27
Replacesfurnace-oil fired steam boiler

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01Problem statement

  • Large hot-water demand. Extraction uses about 5 litres of water per kg of coffee at 90–110 °C, all heated with steam.
  • Evaporator heat rejected. The extract evaporator rejects heat in condensate and condenser water at 45–60 °C.
  • Flavour depends on temperature. Temperature swings in the early columns change extract yield and flavour.
  • Losses between fuel and process. Burning furnace oil in a boiler or heater and distributing the heat loses a quarter or more of the fuel's energy before it reaches the process.
  • Compliance, safety and handling. Fired equipment brings boiler inspections, fuel storage and unloading, flue emissions and an attendant on every shift.

02Use case

The reference plant extracts about 3 tonnes of roast and ground coffee a day in a battery of six columns, with campaigns of instant tea. The extract is concentrated in an evaporator and spray-dried to about 1.2 tonnes of soluble powder. It runs round the clock.

Heat userProcess temp.BasisHeat, kWh/day
Extraction feed water30 → 105 °C3,000 kg coffee × 5 L/kg = 15,000 L/day1,306
Extract preheating before evaporator40 → 75 °C12,000 L/day478
Column jacket losses90–105 °C6 columns × 2 kW × 20 h240
Storage and pipework standing losses–about 5%101
Total useful heat2,125

Averaged over 20 running hours, the heat pumps need about 106 kW.

03P&ID

L-101 · Hot primary · 115 °CTT103L-102 · Return · ~86 °CY-STRP-101AP-101Bduty / standbyEXP-101FS101HP-101…104SE-WWUHT-27 · 27 kWP-100SRC-100extract evaporatorcondensate andcondenser waterheat source ~50 °CWater-sourceTK-1013,500 L115 °CinsulatedventTT101TT102LT101softenermake-up waterVFDP-102A/BL-201 · Supply header · 113 °CTCV-201TIC201PHE-201Extraction water105 °Cwater in 30 °Cto columns 105 °CTCV-202TIC202PHE-202Extract preheater75 °CTCV-203TIC203TK-203Column jackets90–105 °CL-202 · Return header · ~86 °CNCB-001 existing FO boilerstandby / top-up onlyhot supplyreturnsignalsource waterpumpvalvenormally closedINDICATIVE P&ID · NOT FOR CONSTRUCTIONAN-024 · Rev 0 · Sunniva Encon LLP

Tags: HP heat pump, TK tank, SG steam generator, P pump, PHE plate heat exchanger, TCV temperature control valve, TIC temperature indicating controller (panel), TT temperature transmitter, MT moisture transmitter, PT pressure transmitter, LT level transmitter, FS flow switch, NC normally closed. Process fluids are heated through their own exchanger, coil or jacket.

04Solution

System description

  • 4 × SE-WWUHT-27 (108 kW total) (SE-WWUHT water-source, R245fa) delivering 115 °C, covering the day's 2,125 kWh in about 19.7 running hours.
  • A 3,500 L insulated storage tank decouples the heat pumps from the process peaks.
  • Heat source: extract evaporator condensate and condenser water at about 50 °C. Cooling the evaporator condenser water improves vacuum and lowers cooling tower load.
  • The furnace-oil fired steam boiler stays connected behind a normally closed valve as standby.
  • Condensate and condenser water from the extract evaporator, at about 50 °C, are the heat pump source.
  • Extraction feed water is heated to 105 °C on heat pump hot water. Any higher-temperature hydrolysis stages stay on steam.
  • Extract preheating and column jackets run from the same loop.
  • The same system serves instant tea campaigns, which extract at 80–90 °C.

Selected equipment

ModelSE-WWUHT-27 × 4
Heating capacity27 kW each, 108 kW total
COP2.3 estimated for a 50 °C source (the data sheet is rated on a 60/55 °C source)
Ratingwater or steam to 120 °C, R245fa
Supply temperature115 °C
Storage3,500 L insulated tank

Capacity is sized from the heat demand above. COP is an estimate until Sunniva engineering confirms the design.

Control philosophy

TT-101 at the tank top starts the heat pump below 110 °C and stops it at 115 °C. TIC-201 holds extraction water at 105 °C. TIC-202 holds extract at 75 °C before the evaporator. TIC-203 holds column jackets at their set points. If the tank falls below 108 °C, the existing steam heater is enabled as standby.

05Energy saving and ROI

Change any input to match a customer's site. Defaults are typical Indian prices for October 2026. The installed cost is a placeholder; replace it with the actual quotation.

Plant
Existing heating
Heat pump
Annual saving–energy + O&M
Simple payback––
Purchased energy––
10-year net gain–after paying for the system
ExistingHeat pump
Daily consumption––
Annual energy cost––
Cost per tonne of soluble coffee––
CO₂ per year––
Cumulative cash position, years 0–10

06Benefits

Evaporator heat reused

Heat leaving the evaporator heats fresh extraction water.

Steady extraction

Stable feed water temperature helps extract yield and flavour.

Works for tea too

Lower-temperature tea extraction runs from the same hot-water loop.

Lower energy cost

Each kWh of electricity delivers about 2.3 kWh of heat at the required temperature, against well under one kWh of useful heat per kWh of fuel burnt.

No flame on site

No burner, flue or fuel tank for this duty, and no fuel deliveries to schedule.

Built-in redundancy

Several machines share the load. If one is serviced, the others and the storage carry most of the day, with the existing heater in reserve.

07Engineering pointers

Site data to collect

  • Roast coffee and tea extracted per day
  • Extraction water ratio and temperatures by column
  • Evaporator type, condensate and condenser water flows
  • Extract volume and solids
  • Current steam use
  • Present fuel or electricity use and monthly bill
  • Sanctioned electrical load and spare capacity
  • Space for the heat pumps and storage, with service access

Design notes

  • Water quality. Extraction water must be soft and low in chlorine, as both affect flavour and scale the columns.
  • Pressurised loop. At 115 °C the hot-water loop must be held above about 2 bar(g).
  • Aroma recovery. Keep the aroma recovery condenser on its own cooling. Use only the main evaporator streams as the heat source.
  • Source stream. The source must give up roughly two-thirds of the heat delivered. Confirm its flow and temperature over a full production day, and filter it before the evaporator.
  • Water quality. Scale forms quickly above 60 °C. Use softened make-up and keep the heat pump loop closed, with process fluids on the far side of an exchanger or coil.
  • Performance figure. The COP on this page is an engineering estimate, not a data sheet value. Sunniva engineering will confirm it for the actual source and supply temperatures.

Service and warranty

Sunniva has supplied 5,000+ heat pumps since 2012, with nine service technicians across India, including remote sites such as Leh. All components carry a one-year warranty.

Talk to us

sales@sunnivaencon.com+91 93213 65103www.sunnivaencon.com