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Anonymized field reference — engineering experience without publishable raw data

Central China meat plant A: ammonia HP recovers refrigeration heat for plant hot water

Author field survey (2024-05): ammonia mid-temp heat pump coupled to the plant refrigeration train via preheater + condenser-evaporator; plant-reported ~400–500 m³/day hot water displacing purchased steam.

Engineering data

Case type
Anonymized field reference
Data status
anonymized_field_reference
Industry
Food
Source temperature
28–35°C
Sink temperature
55–75°C
Temperature lift
≈ 20 K
Heating or cooling duty
Not disclosed
Architecture
Ammonia mid-temperature heat pump coupled to live refrigeration via preheater + condenser-evaporator + auxiliary receiver liquid path
Result status
Overall operation reported as good; steam purchase displaced for a large share of plant hot-water duty
Key risk
First-year oil change mandatory for the surveyed lubricant grade; piping cleanliness; prefer skid-packaged preheater + condenser-evaporator for future builds
Existing system
Purchased steam for process / sanitation hot water; ammonia refrigeration reject heat available on the discharge / condenser side
Refrigerant
R717 (ammonia)
COP
Not disclosed
Annual savings
Plant-reported: ~¥130k/month (~¥1.56 M/year) steam-cost savings vs purchased steam — not independently metered here
Estimated payback
Plant-reported: CAPEX ~¥2.6 M/set; static payback under ~1.8 years — site-specific tariffs

Project background

A Central China meat-processing plant needed large volumes of process hot water while rejecting ammonia refrigeration heat. The author surveyed the ammonia heat-pump retrofit in May 2024. Customer identity is omitted.

Source / inputs

Source: ammonia discharge / condenser heat via preheater + condenser-evaporator. Sink: plant hot water, plant-reported ~400–500 m³/day. Heating capacity and COP not published as independently metered values on this site.

Heat pump solution

An ammonia mid-temp heat pump evaporates against refrigeration reject heat and delivers heat to the plant hot-water loop. Liquid from the preheater and condenser-evaporator returns via the auxiliary receiver path. Field notes also flag packaging the two exchangers as one skid and simplifying the inlet header for future designs.

COP & savings

Field survey by the author; economics and daily hot-water volume as reported by the plant — not independently metered on this site. HMI snapshots from the visit show the package in normal running status; they are observational evidence only.

Investment / ROI notes

Plant-reported figures: ~¥130k/month steam savings (~¥1.56 M/year) against CAPEX ~¥2.6 M/set, implying static payback under ~1.8 years. Tariffs, hours, and steam price are site-specific; treat as site-reported, not verified ROI.