references · updated 2026-06-29
Zeolite — Adsorbent Families, Numbers & the Low-Regeneration Pivot
confidence: high volatility: warm verified: 2026-06-29fresh
The zeolite adsorbent reference for heat-driven cooling: the material families (classic aluminosilicate 13X/4A/NaY, natural mordenite/clinoptilolite, and the low-regeneration aluminophosphate AlPO/SAPO/AQSOA/EMM-8 class), the numbers (uptake 0.11–0.30 kg·kg⁻¹, heat of adsorption 3300–4400 kJ·kg⁻¹, COP, SCP), the central drawback (classic grades need 150–250 °C regeneration, disqualifying low-grade heat), and the aluminophosphate pivot that brings COP 0.85 down to a 63 °C drive — plus bed engineering, the vacuum constraint, cycle stability, and what actually ships.
Zeolite is one of the core solid sorbents of Adsorption Cooling — a crystalline porous solid that binds a refrigerant vapour (almost always water) on its internal surface, then releases it when heated. It offers higher uptake, specific cooling power, and stability than silica gel, but classic grades pay for it with a high regeneration temperature that locks out low-grade heat. This article is the sorbent-side companion to Performance & Numbers and Composite Salt Sorbents — what zeolite is, the families, the numbers, and why the action has moved to aluminophosphates.
Zeolite belongs unambiguously to the adsorption side of the sorption split: a solid surface sorbent, never a liquid bulk one — see Adsorption vs Absorption. The refrigerant is almost always water (R718); ammonia and methanol pairs exist but are niche.
Material families
| Family | Examples | Water uptake (kg·kg⁻¹) | Regen / desorption temp | Role |
|---|---|---|---|---|
| Classic aluminosilicate | 13X (NaX, FAU), 4A (LTA), NaY | 0.22–0.30 | high, ~150–250 °C | High uptake & stability; the historic workhorse, but too hot for waste heat |
| Natural zeolites | mordenite, clinoptilolite | 0.11–0.12 | high | Cheap, low capacity; mostly of academic interest |
| Silico-/alumino-phosphates | SAPO-34, AlPO, AQSOA Z01/Z02/Z05, EMM-8 | ~0.22–0.28 | low, 60–90 °C | The low-regeneration pivot — high COP on low-grade solar/waste heat |
| Other zeotypes studied | ZSM-5 (MFI) | low–moderate | high | Studied for solar adsorption; underperforms SAPO-34 |
The distinction that matters is classic aluminosilicate vs aluminophosphate, and it is mechanistic, not cosmetic (see below).
The numbers
| Property | Value | Notes |
|---|---|---|
| Water uptake, 13X | 0.30 kg·kg⁻¹ | 4A: 0.22; mordenite/clinoptilolite: 0.11–0.12 (Demir) |
| Heat of adsorption | 3300–4400 kJ·kg⁻¹ | High — the root of the high regen temperature and lower COP (Elsheniti, Demir) |
| Energy density, 13X | ~1290 kJ·kg⁻¹ | Working-pair table, 30–350 °C range (Demir) |
| Desorption range | 70–250 °C | Classic grades effectively need ~150–200 °C (Elsheniti, Kumar) |
| Max cooling COP (classic zeolite/water) | ~0.30 | Anyanwu & Ogueke theoretical max; best of the classic pairs for A/C duty (Al-Yasiri) |
| Single-bed experimental | COP ~0.25, SCP up to 200 W·kg⁻¹ | 5 kW, evap 6.5 °C, 1320 s cycle (Kumar) |
| Mobile double-bed zeolite/water | COP 0.4, SCP 600 W·kg⁻¹ | High SCP, compact (Kumar; [[references/adsorption-performance |
| Thermal-wave two-bed | COP ≈ 1.0 | Internal heat recovery (Elsheniti) |
| Cascade (zeolite/water → AC/methanol) | COP 1.06 | Bridges a large temperature gradient (Dous & Meunier, via Demir) |
| Stratisorp, water–zeolite Li-Y | heating COP 1.98 | 200 °C drive, stratified-storage internal recovery ([[references/adsorption-limitations-and-mitigations |
The central drawback — and the aluminophosphate pivot
Classic zeolites bind water by strong electrostatic interaction with framework cations. That gives a high heat of adsorption (3300–4400 kJ·kg⁻¹) and therefore a high regeneration temperature (~150–250 °C) — which disqualifies low-grade waste heat and low-temperature solar, the very niche adsorption cooling exists to serve (Kumar: “zeolite-water needs ~200 °C”).
The fix is the aluminophosphate (AlPO/SAPO) class, which binds water through a hydrogen-bonded water-cluster mechanism instead of strong electrostatics. The result is an S-shaped (Type V) isotherm — a sharp uptake step over a narrow humidity/temperature window — and a much lower isosteric heat, so the material desorbs at low temperature yet still delivers high uptake:
- EMM-8 (low-cost SFO-topology zeolite-like aluminophosphate, 12-ring channels): uptake 0.28 g·g⁻¹, isosteric heat ~46.76 kJ·mol⁻¹ (barely above water’s 44 kJ·mol⁻¹ heat of vaporisation → easy desorption), regeneration at 65 °C, and a record cooling COP of 0.85 at a 63 °C driving temperature (Liu et al. 2022, Nature Communications). This brings high COP into the waste-heat / low-temp-solar band where silica gel is weak.
- Mitsubishi AQSOA (Z01/Z02/Z05, aluminophosphate zeolite): the commercial OEM adsorbent enabling low-regeneration (<90 °C; Z01 best ~60 °C) machines. Supplied into chillers, not sold as one.
- SAPO-34 beats ZSM-5 in a sun-tracking parabolic-trough rig (max COP 0.169, SCP 169.74 W·kg⁻¹, outperforming ZSM-5 at all adsorption times; Yuan); an SAPO-34/water evacuated-tube unit reached COP 0.575 / EER 5.8 at a 75 °C drive (Al-Yasiri). Recent work engineers directed mass-transfer channels into SAPO-34 to fix intracrystalline diffusion limits (Ammann 2026) — see Fractal / Hierarchical Bed Geometry.
Material selection is not obvious: Tatlier’s “Selection of a favorable zeolite for solar adsorption cooling: how straightforward is it?” argues that the best sorbent depends on the exact drive/sink/chilled temperatures — isotherm shape relative to the operating window matters more than headline uptake.
Engineering constraints
Poor heat and mass transfer. Zeolite beds have low thermal conductivity, the dominant kinetic bottleneck. Mitigations: coated vs packed beds (zeolite coatings on heat-exchanger fins cut thermal mass and improve kinetics — InvenSor’s direct-coated beds are the commercial example), a 3-D graphene binder for zeolite 13X (enhanced conductivity, vapour transport, and uptake kinetics; Gildernew 2022), hydrothermally grown zeolite supports, and copper foams. See Adsorbent Bed Engineering.
Vacuum operation. Water/zeolite runs under high vacuum (water boils at low pressure for the evaporator), an engineering and maintenance burden. NH₃/zeolite avoids the vacuum but runs at 4–11× ambient pressure instead; binary NH₃+H₂O fluids can run near ambient (Demir).
Cycle / hydrothermal stability. Repeated hydration–dehydration can degrade frameworks. A Fraunhofer ISE study profiles cycle stability across silica gels, zeolites, AlPO/SAPO, and MOFs under continuous water-vapour cycling — zeolites and aluminophosphates are generally the hydrothermally robust end relative to many MOFs.
What actually ships
Every commercial adsorption chiller still runs on silica gel or zeolite with a water refrigerant — not lab MOFs (the ~USD 215 M market analysis has zero MOF mentions). See Commercial Adsorption Chillers.
- InvenSor GmbH — direct-coated zeolite + water, the highest catalog COP up to 0.75, plus an HTC line tuned for high-ambient (>40 °C) operation.
- Mayekawa — >70 kW zeolite/water units; locomotive zeolite 13X/water coolers historically (Wolak).
- Mitsubishi Chemical AQSOA — OEM aluminophosphate adsorbent (not a chiller).
- OxiCool Inc. (US Patent 9,765,998 B2) — a zeolite/water two-bed vehicle cooler whose “winterization” configuration stores the water inside the crystalline structure to prevent freeze damage, desorbed by engine exhaust.
- Façade integration: CoolSkin embeds a vacuum zeolite/water adsorber as a switchable solar collector (~54 W·m⁻², up to 150 W·m⁻² best case; Greiner).
- Historically several firms (Zeopower, SunMark, BLM, Solaref) failed to commercialise intermittent zeolite/water units (Wolak).
See Also
-
Building a DIY Adsorption Chiller — activating and charging zeolite/silica in a real bench build (bake-out temps, over-regeneration limits)
-
Adsorption Cooling — the cycle and the heat-driven strategy zeolite serves
-
Performance & Numbers — the full COP/SCP envelope where zeolite sits vs silica gel and MOFs
-
Composite Salt Sorbents — salts impregnated into zeolite 13X / SAPO-34 hosts for 4–5× uptake
-
Limitations & Mitigations — the system-level loss picture and pore-window matching
-
Adsorbent Bed Engineering — coating, consolidating, and conductivity-enhancing zeolite beds
-
Commercial Adsorption Chillers — the vendors shipping zeolite machines
-
Adsorption vs Absorption — why zeolite is a solid-surface sorbent, not a liquid bulk one
Sources
- Liu et al. — Ultralow-temperature water-based sorption refrigeration (EMM-8 aluminophosphate)
- Elsheniti — Adsorption refrigeration technologies
- Kumar — Feasibility of adsorption cooling
- Al-Yasiri — Solar-powered cooling for buildings
- Yuan — Solar adsorption with concentrated collector (SAPO-34 vs ZSM-5)
- Greiner — CoolSkin façade-integrated adsorption cooling
- Barot / OxiCool — Adsorption cooling systems patent (US 9,765,998 B2)
- Demir — Adsorption heat pump problems & solutions
- Wolak — Cooling effect of adsorption/desorption
- Fraunhofer ISE — Cycle stability of sorbents
- Ammann — SAPO-34 directed mass-transfer channels
- InvenSor LTC/HTC datasheets
- Adsorption chillers market
- Zotero cooling registry (review papers: Pérez-Botella, Corma, Tatlier, Freni, Gildernew)