Process & Thermodynamics

Closed-loop heat-pump dehumidification · psychrometric state points · three-stage profile

Read this first — how a heat-pump dryer works (in plain language)

Think of a heat-pump dryer as a dehumidifier running inside a warm, sealed room. Instead of venting moist air to atmosphere (like a conventional dryer, wasting all the heat used to evaporate that moisture), a heat pump captures the moisture as liquid water and reuses the heat to warm the air again. The same air circulates endlessly — dry and hot going in, cool and wet coming out, water squeezed out at the coil, reheated, and sent back. The only energy you pay for is the compressor pumping heat around the loop, plus small losses through the walls.

Hot dry air
62°C / 20% RH
Coconut halves
on trays
Cool wet air
42°C / 71% RH
Evaporator coil
condenses water
Liquid water
drained (862 L)
Reheated to
62°C / 20% RH

The loop never opens — heat and air stay inside. Only water leaves (as liquid) and electricity enters (to drive the compressor).

SMER (Specific Moisture Extraction Rate) — kilograms of water removed per kilowatt-hour of electricity consumed. Higher is better. This design: 4.03 kg/kWh, meaning every kWh of electricity removes 4.03 kg of water. A typical vented gas dryer manages ~1–1.5 kg/kWh.
COP (Coefficient of Performance) — the heat pump delivers COP units of heat for every 1 unit of electricity. At COP 3.2, every kW of electricity moves 3.2 kW of heat from the evaporator to the condenser.

Operating principle (technical)

The dryer is a closed-circuit heat-pump dehumidifier. Hot dry supply air from the condenser passes through the coconut trays, picks up moisture (and cools evaporatively), and returns to the heat pump unit. There, a controlled fraction of the return stream (40% bypass) flows through the evaporator coil, where moisture condenses and is drained as liquid water. The cold, dehumidified stream remixes with the bypass and is reheated by the condenser, closing the loop. Latent heat removed at the evaporator is recycled to the condenser — only the compressor work plus envelope losses must be made up from the electrical supply, which is what gives heat-pump dryers their 3–4× energy advantage over vented hot-air dryers.

State points (design point, stage 2)

StateDescriptionT (°C)RH (%) W (kg/kg)h (kJ/kgda)
3Supply air after condenser 62.020 0.0282136.2
1Return air (wettest trolley) 36.698 0.0380137.8
2Off evaporator (saturated) 16.2100 40.7

Two-stage drying profile (anti-case-hardening)

Shelled coconut kernel is prone to surface sealing if dried too aggressively at low humidity. Stage 1 runs at 55°C for the wet phase (0.9 h, ~30% of water removed); stage 2 ramps to 62°C for 5.2 h to finish. Total: 19.7 h.

Supply temp (top) + fan speed (bottom) across the cycle 55°C 62°C / 70% fan 65°C / 50% fan — deep drying 100% 70% 50% 0 0.9h 6.1h 19.7h
3-stage profile: temperature ramps up (55→62→65°C) while fan speed ramps down (100→70→50%). Fan power ∝ speed³, so the 50% stage uses only 12.5% of full-speed power.

Energy balance & SMER

Water removed per batch862 kg
Peak moisture load (×1.3 stage factor)37.6 kW latent
Evaporator coil duty (design point)94.7 kW
Condenser coil duty88.1 kW
Structure heat loss (PUF 50 mm)1.7 kW
Electric energy per batch214 kWh
SMER (kg water per kWh)4.03 kg/kWh

Validation

The thermodynamic model is cross-checked against an independent Python reference implementation. All 20 computed values match to 3 decimals (relative error < 1%). Sanity ranges pass: drying time in 10–20 h, SMER in 2.5–4.5 kg/kWh, coil outlet above 5°C (no frost risk), return RH < 90%.

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