| HS Code | 720906 |
| Product Name | Extremely Heat-Stable Phytase |
| Enzyme Class | Phytase (myo-inositol hexakisphosphate phosphohydrolase) |
| Ec Number | 3.1.3.8 |
| Source Organism | Engineered bacterial phytase (e.g., Escherichia coli variant) |
| Heat Stability | Retains >90% activity after 90°C for 30 minutes |
| Optimum Temperature | 70°C |
| Optimum Ph | 5.5 |
| Ph Stability Range | pH 3.0 - 8.0 |
| Molecular Weight | ~45 kDa |
| Substrate Specificity | Hydrolyzes phytic acid (myo-inositol hexaphosphate) |
| Activation Ions | Magnesium and calcium ions enhance activity |
| Inhibition | Inhibited by heavy metal ions and high concentrations of phosphate |
| Storage Stability | Stable for 12 months at 25°C in sealed container |
| Activity Unit Definition | 1 FTU releases 1 μmol inorganic phosphate per minute at 37°C and pH 5.5 |
As an accredited Extremely Heat-Stable Phytase factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Packaged in 25 kg polyethylene-lined fiber drums with tamper-evident seals; store dry, away from heat to preserve enzyme activity. |
| Container Loading (20′ FCL) | 20′ FCL container loading: palletized drums of Extremely Heat-Stable Phytase, secured, ventilated, protected from moisture, with safe handling documentation. |
| Shipping | Shipped as a non-hazardous, heat-stable enzyme in sealed, moisture-resistant containers. Ambient temperature transport is acceptable; however, avoid prolonged exposure to extreme heat or humidity during transit. Ensure proper labeling and handling to preserve activity, with standard documentation per chemical shipping regulations. |
| Storage | Store Extremely Heat-Stable Phytase in a sealed, moisture-proof container in a cool, dry, well-ventilated area. Avoid direct sunlight and excessive humidity. Ensure temperatures remain below 25°C for prolonged storage. Minimize air exposure after opening. Under these conditions, product stability and enzymatic activity are preserved until the stated expiration date. |
| Shelf Life | Shelf life: 12 months from manufacture when stored unopened in a cool, dry place, away from direct sunlight. |
In broiler finisher pelleting, compound feed mills subject the 500 FTU/kg complete-feed dose of an extremely heat-stable phytase to a short but wet thermal event: meal entering the conditioner at 25°C and 13–14% moisture is exposed to steam at 80–85°C for 45–90 s, raising moisture to 15–18% before compression through a 3.0–3.5 mm pellet die with compression ratio 10–12. The regulatory anchor for this downstream segment is Regulation (EC) No 1831/2003 Annex I category (d) zootechnical additives, functional group 4a digestibility enhancers, with in-process activity verification performed according to ISO 30024:2009; the finished-feed mill is also expected to operate under Regulation (EC) No 183/2005 HACCP-based feed hygiene procedures. Formulation addition rates in broiler finisher diets span 250–1,000 FTU/kg complete feed, with 500 FTU/kg selected when the matrix removes 0.10% available phosphorus and 0.10% calcium; adoption of a larger matrix at 500 FTU/kg requires a mill-specific recovery trial because published data for conditioner configurations above 85°C is limited. Downstream production begins with grinding through a 3.0 mm hammer-mill screen, followed by batch mixing in a double-ribbon mixer with dry mixing time 180–240 s and coefficient of variation no greater than 5%; the enzyme is introduced through a micro-dosage system as a dry premix or granulate, not through the post-pelleting liquid coater. Steam conditioning at 2.0–2.5 bar then brings meal to the stated outlet temperature before pelleting, and cooling on a horizontal belt cooler reduces pellet temperature to 20–30°C. The terminal product is a 3.0–3.5 mm broiler finisher pellet with 12–13% moisture. Process audits on production-scale lines show that residual phytase activity varies more with steam pressure fluctuation than with short cold start-up; steam slugging or condensate carryover in the conditioner can produce batch-to-batch retention deviations above ±8%. The operational boundary is therefore stated as conditioner outlet ≤85°C and residence time ≤90 s, and the enzyme should not be held in acidified liquid solution or combined with aggressive mineral premix carriers in the same dosing stream.
Swine grower-finisher mash lines operate at lower nominal temperatures than broiler pelleting, but the thermal risk is not absent because wet heat in a conditioner depends on time and moisture as well as steam temperature. The applicable compliance framework for intra-EU movement is Regulation (EC) No 1831/2003, Annex I category (d), functional group 4a, with activity checked by ISO 30024:2009; feed safety management under GMP+ BA2 and Regulation (EC) No 183/2005 is typically required by buying groups. Formulation addition rates for grower-finisher pig diets are 250 FTU/kg for standard-phase feeds and 500 FTU/kg when formulating low-phosphorus finisher diets with a matrix of 0.08% available phosphorus and 0.08% calcium. In downstream production, the enzyme is mixed into the dry portion in a twin-shaft paddle mixer, and the batch is then conditioned at 65–75°C for 20–40 s before passing an annular gap expander at 85–90°C for 5–10 s or proceeding directly to a pellet press with a 3.5–5.0 mm die and compression ratio 8–12. The finished terminal product is a 3.5–5.0 mm swine grower-finisher pellet or a coarse meal, with fat added post-pelleting at 5–7% by spray drum coater. The limit of dry heat-free storage does not eliminate the risk of moist-heat inactivation inside the expander; if the expander outlet exceeds 90°C, the enzyme must be sampled before and after the expander at least once per shift, and the condition is considered outside the normal operating boundary because retention falls more steeply above this point.
| Standard / Regulation | Scope | Relevant Designation |
|---|---|---|
| Regulation (EC) No 1831/2003 | Authorisation of zootechnical feed additives | Annex I category (d), functional group 4a |
| ISO 30024:2009 | Phytase activity in animal feeding stuffs | In-plant retention testing |
| Regulation (EC) No 183/2005 | Feed hygiene requirements | HACCP-based procedures |
| FDA 21 CFR Part 507 | Current Good Manufacturing Practice for animal food | Subparts B–E |
| AAFCO Official Publication | Enzyme preparation feed terms | Official feed terms |
| CAC/RCP 54-2004 | Code of Practice on Good Animal Feeding | Good feeding practice |
In extruded aquafeed production for tilapia, carp, and whiteleg shrimp, the enzyme may pass through a twin-screw extruder with barrel temperatures above 120°C and then through a hot-air dryer before final coating, creating a fundamentally different thermal damage mechanism from pelleting. The regulatory baseline is Regulation (EC) No 1831/2003 Annex I category (d), functional group 4a, combined with Codex Alimentarius CAC/RCP 54-2004 for good animal feeding practice and ISO 30024:2009 for activity assay; for shrimp feed entering global supply chains, the feed-safety management system is usually certified against ISO 22000:2018 or equivalent. Addition rates for low-fishmeal aquafeed formulations containing 40–60% soybean meal or soy protein concentrate range from 500 FTU/kg to 2,000 FTU/kg complete feed, with the higher doses used when phytate phosphorus occupies more than 0.35% of dry matter and the phosphorus replacement matrix exceeds 0.10% available phosphorus. Downstream production typically uses a preconditioner at 90–95°C for 120–180 s, a twin-screw extruder with L/D 24–32, barrel profile 120–135°C, die pressure 20–60 bar, and specific mechanical energy input 25–40 kWh/t; extrudate moisture at 25–30% is then reduced in a dryer at 90–100°C for 15–25 min, and oil or fat is applied in a vacuum coater at 0.8 bar absolute pressure. The terminal product is a 2.0–4.0 mm extruded sinking pellet or a 3.0–6.0 mm floating pellet with 60–120 min water stability, depending on bulk density control through screw speed and die configuration. Pre-extrusion addition at barrel temperatures above 125°C may yield activity losses exceeding 50%; published retention data for this specific configuration is limited, so post-extrusion vacuum coating of the enzyme is preferred when barrel temperature cannot be reduced. If the enzyme is applied post-extrusion, the liquid suspension must be metered through a high-precision pump onto the vacuum coater after the fat addition step to avoid hydrophobic film interference, and the coating system must produce a dose coefficient of variation below 10%.
Dry pet food extrusion differs from poultry pelleting because the mash is plasticised under high shear and then dried at belt temperatures that would not normally be used for feed enzymes. Compliance for dog and cat kibble marketed in North America is anchored to FDA 21 CFR Part 507 Subparts B–E for CGMP, with enzyme preparations listed under AAFCO Official Publication feed terms; in the EU, the same product is regulated under Regulation (EC) No 1831/2003 and labelled according to Regulation (EC) No 767/2009. Addition rates in complete dry kibble formulations are 250–750 FTU/kg, commonly 500 FTU/kg, with a phosphorus matrix of 0.08% available phosphorus and 0.08% calcium at the 500 FTU/kg dose. Downstream production starts with preconditioning at 90–95°C for 60–120 s, followed by single- or twin-screw extrusion at barrel temperature 120–150°C, die pressure 40–80 bar, and specific mechanical energy 60–90 kWh/t; the resulting wet extrudate is dried on a belt dryer at 120°C for 15–20 min to reach <10% moisture and water activity below 0.65. The terminal product is a dry extruded dog or cat kibble, usually coated with fat and palatant after cooling. In high meat inclusion formulas containing 30–40% fresh meat slurry, the water and fat phase at the preconditioner increases the wet heat load; therefore pre-extrusion phytase addition is controlled at the preconditioner outlet rather than the extruder barrel. If the barrel profile must exceed 150°C, pre-extrusion dosing becomes the critical control point and process validation under ISO 30024:2009 is required; otherwise a post-dryer liquid enzyme coating may be used, but the coating pump must deliver a uniform dose on kibbles with coefficient of variation below 10% and the enzyme must not be premixed with acidulated palatant.
Layer crumble lines combine moderate heat with high dietary limestone, which changes the phytate hydrolysis environment in the bird and makes the selection of an extremely heat-stable phytase less about pelleting temperature and more about consistent release of phytate phosphorus in a high-calcium digesta. Compliance for layer feed in Europe is Regulation (EC) No 1831/2003 Annex I category (d), functional group 4a, with activity verification by ISO 30024:2009; GMP+ BA2 or equivalent feed safety assurance is often mandatory in export-oriented mills. Addition rates are 300–600 FTU/kg complete layer diet, with 400 FTU/kg used in formulations where total calcium is 3.8–4.2% and available phosphorus is reduced by 0.08%. The manufacturing route is mixing in a batch ribbon mixer, steam conditioning at 70–80°C for 30–60 s, pelleting through a 3.0 mm die, crumbling between rolls set at 1.5–2.5 mm gap, and sifting to remove fines below 1.5 mm. The terminal product is a 1.5–3.0 mm layer crumble with 3.5–4.0% calcium and 0.30–0.40% available phosphorus. The operational boundary is conditioner outlet ≤80°C for ≤60 s; above this, phytase activity may still survive, but the combination of limestone, long conditioner residence time, and fluctuating steam quality creates an avoidable wet-heat denaturation risk. Calcium itself inhibits phytase in the gastrointestinal tract; therefore the heat-stability claim does not permit increasing the calcium matrix without a corresponding in vivo phosphorus digestibility validation.
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The product designated EHSP-10G is a granular 6-phytase preparation with a declared minimum activity of 10,000 FTU/g determined by ISO 30024:2009. The enzyme is produced by submerged fermentation of a fungal donor strain and is formulated as a coated microgranule for dry addition to compound feed prior to steam conditioning and pelleting. The catalytic function is the sequential hydrolysis of myo-inositol hexakisphosphate to lower inositol phosphates and inorganic phosphate, with the first cleavage occurring preferentially at the C6 position. The preparation is intended for monogastric feed applications in which intrinsic phytate-bound phosphorus is converted to absorbable inorganic phosphorus. Typical in-feed targets range from 250 FTU/kg in layer diets to 1,000 FTU/kg in piglet creep feeds, with the final dose dependent on dietary calcium-to-phosphorus ratio, phytate substrate load, and pellet conditioning severity. The granular formulation exhibits a bulk density of approximately 0.65 kg/L and a particle size distribution in which not less than 90% by mass is retained between 250 µm and 850 µm sieves, allowing homogeneous dispersion in premixes and compound feeds during low-inclusion dry blending.
The heat-stable designation refers to retention of catalytic activity after hydrothermal treatment rather than intrinsic thermophilicity of the free enzyme. The formulated granule contains an inorganic salt buffer and a hydrophobic coating that delays moisture ingress during the conditioner dwell time. Denaturation onset in differential scanning calorimetry is therefore not equivalent to the midpoint of unfolding of the uncoated enzyme; the apparent inactivation boundary is shifted by the coating and by the rapid evaporative cooling after the die plate.
Survival data are normally generated on production-scale systems rather than laboratory ovens, because dry heat and steam conditioning act through different inactivation kinetics. A split-plot feed mill evaluation using a horizontal paddle conditioner with 45 s barrel retention, a 4.0 mm die by 60 mm effective thickness, and a counterflow pellet cooler was conducted at conditioner outlet temperatures of 80°C, 85°C, 90°C, and 95°C. Feed was a maize–soybean meal broiler grower with 12.0% added moisture at the mixer and 2.2 bar steam pressure. Post-pellet activity was extracted from freeze-milled pellet samples passing a 0.5 mm sieve and assayed by ISO 30024:2009.
| Conditioning temperature and retention time | EHSP-10G residual activity | Conventional uncoated 6-phytase residual activity | Conventional coated 3-phytase residual activity |
|---|---|---|---|
| 80°C, 30 s | 96% | 58% | 72% |
| 85°C, 30 s | 92% | 41% | 61% |
| 90°C, 30 s | 84% | 24% | 47% |
| 95°C, 30 s | 71% | 11% | 28% |
Steam moisture, not temperature alone, is the dominant inactivation vector. Dry heating of the same granule in a ventilated oven at 95°C for 30 min produced a residual activity above 90%, confirming that condensation onto the coating during conditioning is the critical event leading to enzyme release and denaturation. Conditioner meal moisture above 16.5% is therefore a process limit; above this value, survival falls by approximately 8–12 percentage points for each additional 1.0% moisture at constant temperature. Retention time variability of ±5 s in a paddle conditioner produced a 7 percentage point range in post-pellet activity across production shifts. Inactivation during conditioning follows apparent first-order kinetics over the first 60 s of wet heat exposure. The calculated inactivation rate constant for EHSP-10G at 90°C and 16.0% meal moisture is approximately 0.005 s−1; for an uncoated 6-phytase control under identical conditions, the corresponding value is approximately 0.021 s−1. The apparent activation energy of inactivation in the coated granule is 145 kJ/mol, compared with 112 kJ/mol for the uncoated enzyme. These values are derived from internal retention samples and are single-trial representative ranges, not guaranteed specifications.
Batch release for EHSP-10G follows the analytical profile below. The product is certified for dry addition to complete feed and premixtures and is shipped in 25 kg multi-wall paper sacks with a polyethylene liner. Storage stability data indicate a loss of not more than 10% of declared activity after 12 months at 25°C in unopened packaging. The coated microgranule is produced by concentration of the fermentation broth by ultrafiltration, followed by spray granulation onto a salt-starch core and fluidized-bed coating with a hydrophobic matrix. Coating integrity is assessed by a dissolution test in 0.08 mol/L acetate buffer at 40°C; after 10 min, less than 15% of declared activity is released.
| Parameter | Limit | Analytical method |
|---|---|---|
| Declared phytase activity | ≥10,000 FTU/g | ISO 30024:2009 |
| Moisture | ≤8.0 g/100 g | ISO 6496:1999 |
| Particle size 250–850 µm | ≥90% | Sieve analysis per ISO 2591-1 |
| Lead | ≤10 mg/kg | EN 17053:2018 |
| Arsenic | ≤3 mg/kg | EN 17053:2018 |
| Cadmium | ≤1 mg/kg | EN 17053:2018 |
| Mercury | ≤0.1 mg/kg | EN 17053:2018 |
| Salmonella | absent in 25 g | ISO 6579-1 |
| Escherichia coli | ≤10 CFU/g | ISO 16649-2 |
| Dustiness | ≤0.5 mg/g | Stauber-Heubach dust meter |
The Stauber-Heubach dust value is assessed on the undiluted granule; in a premixture at 10% enzyme concentration, the dust fraction is below the detection limit of the same method.
In feed mills operating with conditioner outlet temperatures of 85–90°C, post-pellet liquid phytase application has historically been used to avoid thermal inactivation. With EHSP-10G, dry addition at the mixer is feasible because post-pellet survival at 90°C remains above 80% under the process conditions specified above. This removes the need for post-pellet metering pumps, spray nozzles, and liquid enzyme storage lines on twin-shaft paddle mixers with batch capacities between 250 kg and 2,000 kg or continuous mixers processing 20 t/h.
Mixer addition should be made after the dry minerals and before the addition of liquid fat. A dry mixing time of 120 s at a mixer fill factor of 60% gives a coefficient of variation below 10% for enzyme activity in ten grab samples. If the mixer fill factor exceeds 80%, the required mixing time is extended to 180 s because axial dispersion is reduced in overfilled chambers. In a twin-shaft mixer with 2,000 kg batch size, adding 100 g of EHSP-10G per batch achieves 500 FTU/kg before pelleting. For smaller batch mixers of 250 kg, the weight addition is 12.5 g per batch, which requires a micro-ingredient scale with accuracy of ±0.1 g.
Target in-feed activity after pelleting should be confirmed by extraction and assay. In broiler grower diets with 0.85% calcium and 0.38% available phosphorus, a target of 500 FTU/kg is typical. The pre-pellet dose is calculated by dividing the target by the expected thermal survival fraction at the highest conditioner temperature. At 90°C and 30 s retention, a pre-pellet dose of 600 FTU/kg provides a post-pellet measured activity of approximately 504 FTU/kg, using the 84% survival fraction. At 95°C, the pre-pellet dose is raised to 700 FTU/kg to maintain approximately 497 FTU/kg after pelleting. Overdosing above 2,000 FTU/kg does not linearly release additional phosphorus; the phytate hydrolysis curve approaches saturation because substrate accessibility and gastric retention time become limiting. Matrix values for phosphorus replacement should be assigned only after in vivo ileal digestibility or performance validation. Published comparative literature on 6-phytases indicates that 500 FTU/kg can replace 0.10–0.12% available phosphorus depending on calcium and phytate content, but batch-level feed formulation changes require confirmation under the specific dietary context.
EHSP-10G exhibits a pH activity profile that differs from most 3-phytase preparations from Aspergillus niger. The 6-phytase retains at least 70% of maximum activity between pH 2.5 and pH 5.5, whereas a conventional 3-phytase reference shows a sharp decline below pH 3.0. After incubation for 120 min in simulated gastric fluid containing 2,000 U/mL porcine pepsin at pH 2.0 and 37°C, the 6-phytase retains 65–75% of initial activity, compared with 25–40% for a typical uncoated 3-phytase. The broader pH window is relevant in the broiler proventriculus and gizzard, where luminal pH ranges from 2.8 to 4.5 before neutralization in the small intestine. The difference arises from the active-site architecture of 6-phytase and from glycosylation extent, not from a simple shift in isoelectric point.
In comparison with a coated 3-phytase product, EHSP-10G also shows a lower early release of active enzyme in the mash stage. This reduces activity loss during preconditioning but can delay initial hydrolysis in the crop. In poultry assays, the delay is not biologically significant at standard dosages because proventricular residence time exceeds 45 min. Published data for this specific formulation in non-standard species is limited; for duck and turkey, additional validation is required.
EHSP-10G should not be incorporated into acidified premixes containing free organic acids at concentrations above 10% before dilution into final feed. Premix moisture above 13.5% requires drying before enzyme addition to prevent premature coating disintegration. The granule coating is incompatible with long-chain aldehyde-based sanitizers used in liquid post-pellet application lines; if post-pellet liquid phytase or other enzymes are used simultaneously, separate flushing with demineralized water is required. The bagged product should be stored at or below 25°C and protected from moisture. Opened sacks should be consumed within 30 days to prevent activity loss above the specified 10% storage limit. The product is not recommended as the sole phytase source in extruded aquafeed processed above 105°C barrel temperature and 22% moisture because the combined hydrothermal residence time exceeds the coating tolerance; published data for this specific configuration is limited. Batch-to-batch variation in post-pellet survival is below 5 percentage points when assayed by ISO 30024:2009 on cooled pellet samples, based on internal retention data.
One production-scale failure mode observed with dry phytase addition is incomplete enzyme extraction from pellets. If pellets are not freeze-milled below 0.5 mm before assay, apparent activity can understate actual survival by 15–20%. This analytical artifact is excluded by applying the full extraction protocol of ISO 30024:2009 to frozen, ground pellet samples. In compound feed containing choline chloride as a separate granule, physical segregation can occur if the particle size difference exceeds 300 µm; segregation testing using a six-section mixer sampling probe is recommended. The product is not classified as hazardous under REACH or GHS in the as-supplied solid form, but respiratory protection for dust exposure is required when handling the undiluted granule at levels above 10 mg/m³ inhalable dust. The granule is stable to 60°C dry storage for 4 weeks without loss, but pallet storage in direct sunlight should be avoided because sack surface temperatures can exceed 50°C even at ambient air temperatures below 30°C.