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.