| HS Code | 774109 |
| Productname | Sinopec Qilu mLLDPE QHM22F |
| Polymertype | Metallocene linear low-density polyethylene |
| Density | 0.922 g/cm³ |
| Meltflowrate | 2.0 g/10 min (190°C/2.16 kg) |
| Meltingpoint | 118 °C |
| Vicatsofteningpoint | 95 °C |
| Tensilestrengthatyield | 10 MPa |
| Tensilestrengthatbreak | 30 MPa |
| Elongationatbreak | 500 % |
| Dartimpactstrength | 200 g |
| Tearstrengthmd | 100 N/mm |
| Tearstrengthtd | 200 N/mm |
| Haze | 8 % |
| Gloss | 80 % |
As an accredited Sinopec Qilu mLLDPE QHM22F factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Sinopec Qilu mLLDPE QHM22F is supplied in 25 kg woven bags, with each bag containing 25 kg. |
| Container Loading (20′ FCL) | 20′ FCL container loaded with palletized Sinopec Qilu mLLDPE QHM22F bags, shrink-wrapped, strapped, and secured for ocean freight. |
| Shipping | Sinopec Qilu mLLDPE QHM22F is typically shipped in 25 kg moisture-proof PP/PE bags with inner liners, palletized or loaded loose in 20'/40' containers by sea. Store in a dry, ventilated area away from direct sunlight, heat, and moisture. |
| Storage | Store Sinopec Qilu mLLDPE QHM22F in a cool, dry, well-ventilated warehouse, protected from direct sunlight, rain, moisture, and heat sources. Keep original bags sealed, clean, and palletized; avoid tearing, contamination, and contact with oils, acids, alkalis, and oxidizers. Keep away from ignition sources and incompatible materials. Follow supplier SDS, stacking limits, and shelf-life recommendations. |
| Shelf Life | Shelf life is 24 months when stored in original, unopened packaging in a cool, dry, well-ventilated area, away from direct sunlight. |
In three-layer food packaging structures produced on high-speed vertical form-fill-seal lines, the sealant web is the throughput-limiting layer. A converter evaluating QHM22F in that position must first verify lot-specific melt mass-flow rate by ISO 1133-1:2022 and density by ISO 1183-1:2019, because metallocene LLDPE lots with identical nominal melt index can differ in shear viscosity and seal response. The sealant layer is commonly blended at 70 wt% QHM22F with 30 wt% LDPE having density 0.923–0.925 g/cm³ and melt mass-flow rate 0.3–0.7 g/10 min; the LDPE component lowers extruder head pressure and stabilizes the bubble but raises seal initiation temperature by 2–5 °C relative to the neat mLLDPE. Seal strength is measured under ASTM F88/F88M-21 using a 25 mm wide specimen, 0.3 MPa jaw pressure, 0.5 s dwell, and 300 mm/min separation speed; converters of dry soup sachets often require a minimum seal strength of 12 N/15 mm at 115 °C. Hot tack is measured under ASTM F1921-18 after 0.2–0.5 s cooling; the hot-tack plateau should remain above 2 N/15 mm across 105–125 °C to tolerate jaw-temperature fluctuation on a 120 pouch/min line. On a five-layer blown film line with 65 mm extruders, melt temperature is normally kept at 195–210 °C, die gap at 2.0–2.5 mm, and blow-up ratio at 2.5:1; if die pressure exceeds 35 MPa, addition of a fluoropolymer processing aid at 200–800 ppm active is used to lower melt fracture risk. Food-contact compliance must be confirmed for the specific food simulant: EU 10/2011 overall migration limit is 10 mg/dm² for the final article, and FDA 21 CFR 177.1520 establishes olefin polymer conditions of use. Amine-based antistatic additives should be avoided in this layer unless the supplier provides a specific migration limit for the exact amine. The finished articles include pillow packs for frozen vegetables, sachet films for dry soups, and sealed pouches for grated cheese.
Heavy-duty sacks for pelletized resin, fertilizer, and dry construction chemicals are produced as 3-layer or 5-layer coextruded blown film at total thickness from 80 µm to 160 µm. The mLLDPE-containing core influences dart impact retention and tensile elongation, while high-density polyethylene surface layers control stiffness and coefficient of friction. A trial formulation may use 40 wt% QHM22F in the core with 60 wt% HDPE or Ziegler-Natta LLDPE, but published data for this specific QHM22F configuration is limited. The film is processed with die gap 1.8–2.5 mm, blow-up ratio 2.2–3.0, and frost line height adjusted to 8–12 times the die gap. Dart impact is measured by ISO 7765-2 or ASTM D1709-16A; a 100 µm film for fertilizer sacks often must meet an end-user specification of ≥600 g, but converter trials should establish the actual QHM22F value. Elmendorf tear is measured by ISO 6383-2; machine-direction tear may be lower than transverse-direction tear in high-draw films. Surface coefficient of friction measured by ISO 8295 should be controlled between 0.20 and 0.35 to prevent pallet slippage. Creep under constant load at 40 °C for 7 days is often specified for resin pellet export sacks, with extension below 15% as a common acceptance limit. Non-food sacks require REACH and RoHS declarations from the final article supplier; food ingredient sacks, where used, require EU 10/2011 and FDA 21 CFR 177.1520 documentation. End products include valve sacks, open-mouth sacks, and form-fill-seal heavy-duty bags.
When agricultural greenhouse and low-tunnel cladding producers incorporate QHM22F into three-layer film, the focus shifts from seal performance to long-term tensile retention and tear balance under ultraviolet exposure. Greenhouse film builds typically use 120–200 µm total thickness with an outer layer containing UV absorbers, a middle layer containing QHM22F and hindered amine light stabilizer, and an inner layer containing antifog and anti-drip additives. The mLLDPE component can raise tensile elongation at break measured by ISO 527-3:2018, but the converter must verify that the final stabilized film retains at least 50% of initial tensile strength after 3,000–5,000 h of accelerated weathering under ISO 4892-2 or ASTM D2565-21. The blown film line is typically operated with die gap 2.0–2.8 mm and blow-up ratio 2.5–3.5 to achieve balanced MD/TD tear resistance. Haze is measured under ISO 14782 or ASTM D1003-21; for greenhouse cladding, light transmission is controlled primarily by the UV and antifog package rather than the base resin. Slip and antiblock packages should be kept low, usually 1,000 ppm active silica and 500 ppm erucamide, because high additive loadings reduce light transmission. Batch-to-batch variation in mLLDPE comonomer distribution may alter crystallization rate during bubble collapse; therefore, frost line height and bubble diameter should be logged against every lot. End products include multi-season greenhouse cover film, low tunnel cladding, and nursery liner film.
Individually quick-frozen food packaging runs on vertical form-fill-seal machines under low ambient temperatures, where seal integrity is challenged by product fines on the seal area. The sealant layer containing QHM22F is evaluated for cold-temperature impact after conditioning at -20 °C for 24 h, using ISO 7765-2 or ASTM D1709-16A. Seal strength is measured under ASTM F88/F88M-21 at ambient temperature after film conditioning, and hot tack under ASTM F1921-18; low-temperature seal strength testing is not standardized, so converters often apply an internal method with 5 mm/min peel speed at -10 °C. The layer structure commonly places QHM22F in the sealant layer at 70–80 wt% with LDPE or polyolefin plastomer as diluent to lower seal initiation temperature. The outer layer may be high-density polyethylene or propylene copolymer for abuse resistance. The finished bags are filled with frozen peas, corn, mixed vegetables, or seafood. Product contamination on the seal area reduces hot tack; to compensate, the sealant formulation may include 10–20 wt% polyolefin plastomer with seal initiation below 90 °C, but published data for QHM22F blends in this exact configuration is limited. Extrusion conditions use die gap 2.0–2.5 mm, melt temperature 185–200 °C, and blow-up ratio 2.0–2.5 to avoid excessive film blocking. Compliance follows EU 10/2011 and FDA 21 CFR 177.1520 when the final film contacts food.
Under pallet unitization conditions, cast stretch film containing QHM22F in the core or back layer changes pre-stretch ratio and cling response. The machine-direction prestretch is typically operated at 200–300% on power pre-stretch carriages, and the core resin must withstand elongation without puncture. The film structure is usually a 3-layer cast coextrusion with skin layers of low-density polyethylene or EVA for cling and release. QHM22F may be used in the core at 60–80 wt% with LDPE or polyolefin plastomer diluent. The film tensile elongation at break is measured by ISO 527-3:2018 or ASTM D882-18; films of 20 µm nominal thickness often require machine-direction elongation greater than 350%. Puncture resistance is measured by ASTM D5748-19; converters must establish baseline data for QHM22F because published comparative data for this specific core configuration is limited. Cling is measured by ASTM D5458-95 or ISO 8295, and unwind force must remain below 8 N/25 mm to prevent stretched-wrap feedback on high-speed wrappers. The outer release layer includes slip additives to control blocking, while the cling layer includes polyisobutylene or EVA with vinyl acetate content 28–33 wt%. The final products include machine wrap, hand wrap, and agricultural silage stretch film, each requiring a different balance of cling and puncture resistance.
Collation shrink film for bottled water, canned goods, and beverage multipacks uses mLLDPE to improve sealability and shrink force while maintaining clarity. The film is produced on high-stalk or low-stalk blown film lines at thicknesses of 30–80 µm, with die gap 1.6–2.0 mm and blow-up ratio 4.0–5.5 to generate high transverse-direction orientation. The high blow-up ratio increases transverse shrink, which is necessary for sleeve and shrink-film applications. QHM22F may be blended with LDPE and medium-density polyethylene at 30–50 wt% to balance shrink force and seal strength. Shrink properties are measured by ISO 14616 or ASTM D2732-14 using a 120 °C oil bath; transverse-direction shrink is typically 50–70% for high-shrink collation film, but converter data for QHM22F is required. Seal strength is tested by ASTM F88/F88M-21; the seal must remain intact through shrink tunnel temperatures of 160–200 °C. The film must avoid burn-through during sealing; hot tack measured under ASTM F1921-18 is critical because the film is sealed under high-speed continuous motion. Haze is measured under ISO 14782; product visibility requires haze below 10% for 30 µm film, depending on the final specification. End products include printed collation shrink sleeves, unsupported shrink wrap, and shrink bundles for beverage cans.
High-clarity overwrap for boxed chocolate, cosmetics, and personal care products is a conversion where QHM22F must combine low haze, low seal initiation, and minimal gel count. The film is typically produced as a 20–40 µm cast or blown monolayer or coextruded structure. Seal initiation temperature is evaluated by sealing at 5 °C intervals from 90 °C to 125 °C under ASTM F88/F88M-21; the film must achieve 2 N/15 mm at the lowest practical temperature. Haze is measured under ISO 14782; high-clarity overwrap often requires haze below 6% at 30 µm. Gel count is inspected with an optical film analyzer; QHM22F lot consistency must be verified because gel seeds can produce visible defects on printed overwrap. The line is run with die gap 1.6–2.0 mm, blow-up ratio 2.5–3.0, and melt temperature 190–205 °C. Slip and antiblock levels are kept low, 500–1,000 ppm active silica or talc, to avoid haze increase. End products include overwrap for gift boxes, cosmetics cartons, and stationery sets. Compliance for non-food contact requires REACH and RoHS declarations, while food-contact overwrap requires EU 10/2011 and FDA 21 CFR 177.1520.
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Sinopec Qilu mLLDPE QHM22F is a metallocene-catalysed linear low-density polyethylene resin produced by Sinopec Qilu Petrochemical Company for blown-film extrusion. The resin is supplied as free-flowing pellets; release documentation includes a nominal melt mass-flow rate of 2.0 g/10 min determined at 190 °C with a 2.16 kg load in accordance with ISO 1133-1:2022, and a nominal density of 0.918 g/cm³ determined in accordance with ISO 1183-1:2019. The single-site metallocene catalyst architecture produces a narrow molecular-weight distribution and a more uniform short-chain branching distribution than conventional Ziegler-Natta linear low-density polyethylene. Lot-specific certificates of analysis govern actual release values for melt flow rate, density, comonomer content, antioxidant concentration, and gel count. Published data for this specific Qilu grade configuration is limited in accessible trade literature; therefore, processing and comparative property statements below are based on the metallocene LLDPE class and should be confirmed on target production equipment.
The process difference originates in molecular-weight distribution. QHM22F is expected to exhibit a polydispersity index in the range of 2.0–2.5 by gel permeation chromatography with linear polyethylene-equivalent calibration. The reduced high-molecular-weight tail lowers shear thinning compared with broad-distribution Ziegler-Natta LLDPE. On a grooved-feed single-screw extruder with an L/D ratio of 25:1 to 30:1 and a barrier screw designed for linear polyethylene, barrel temperatures from feed to adapter are typically set at 170–210 °C, while the die zone is held at 190–210 °C. Measured melt temperature should remain below 230 °C; residence times above 10 min at such temperatures can initiate chain scission and gel formation. Under these conditions, bubble formation is stable at blow-up ratios of 2.0:1 to 2.5:1 with a die gap of 1.2–2.0 mm and a frost-line height of 100–200 mm above the die face. Output-rate limits are often governed by the onset of sharkskin melt fracture rather than by motor load. If sharkskin appears at high die shear, increasing the die lip temperature by 5–10 °C or widening the die gap usually suppresses the disturbance. A fluoropolymer processing aid at 200–500 mg/kg is also effective; it should be added via masterbatch and allowed to condition the die surface before film collection.
Because the resin has lower melt strength than high-pressure LDPE at equivalent melt index, bubble stability under high blow-up ratio or deep-draw conditions may be reduced. Blending 5–15 wt% high-pressure LDPE raises extensional viscosity and stabilizes the bubble but can increase haze and reduce dart impact. The specific trade-off is line-dependent and should be mapped with a full-factorial trial at the target gauge.
Blown-film property data reported for metallocene LLDPE grades with density 0.918 g/cm³ and melt flow rate 2.0 g/10 min show a characteristic shift relative to conventional Ziegler-Natta C4-LLDPE. Dart drop impact measured to ASTM D1709-16a, Method A, on 50 µm film is typically 30–50% higher than that of Ziegler-Natta C4-LLDPE at equal gauge. Elmendorf tear measured to ASTM D1922 is commonly lower in the machine direction and higher in the transverse direction because the narrower distribution reduces orientation hardening during blowing. Haze determined by ASTM D1003-13 on 40 µm film is usually below 10%; gloss at 45° under ISO 2813:2014 is usually above 60 GU for the class. Tensile yield strength in the machine direction according to ISO 527-3:2018 on 25 µm film is typically 9–12 MPa, and elongation at break commonly exceeds 400%. These values are class-typical and are not a substitute for lot-specific data generated under the same die geometry, frost-line height, and take-off speed used in production.
The property differences of QHM22F as a metallocene LLDPE arise at the microstructural level. A uniform short-chain branching distribution prevents the formation of the broad composition fluctuations that are characteristic of heterogeneous Ziegler-Natta resins. Because short-chain branches are more evenly distributed across both high- and low-molecular-weight chains, the average inter-lamellar tie-molecule density increases at a given density and molecular weight. This structural difference raises slow-puncture and dart drop impact without requiring a large increase in density or a loss of optical clarity. The lower optical haze is similarly linked to the reduction in composition fluctuations that create light-scattering domains in Ziegler-Natta LLDPE. However, the same narrow distribution reduces the strain-hardening component of extensional viscosity; this is why melt strength and planar bubble stability are lower than in branched LDPE and why film processors may observe more stable operation after adding a branched LDPE fraction.
The following table lists the primary specification parameters and test designations used for polyethylene film resins. Nominal values are stated for QHM22F; mechanical and optical values are class-typical ranges unless a lot-specific certificate of analysis is provided.
| Parameter | Test designation | Value |
|---|---|---|
| Melt mass-flow rate | ISO 1133-1:2022, 190 °C, 2.16 kg | 2.0 g/10 min |
| Density at 23 °C | ISO 1183-1:2019 | 0.918 g/cm³ |
| Polydispersity index | GPC, linear PE calibration | 2.0–2.5 |
| Dart drop impact, 50 µm film | ASTM D1709-16a, Method A | Class-typical 30–50% higher than C4 Z-N LLDPE |
| Haze, 40 µm film | ASTM D1003-13 | ≤10% class-typical |
| Gloss at 45° | ISO 2813:2014 | ≥60 GU class-typical |
Mechanical and optical data are application-dependent. Film property values shift with gauge, blow-up ratio, frost-line height, and cooling-air temperature; direct comparison between film samples therefore requires identical processing history. Release limits for the product are governed by the manufacturer’s certificate of analysis and should be reviewed for each incoming lot.
Application feasibility for QHM22F covers high-integrity food packaging, lamination structures, heavy-duty sacks, and agricultural greenhouse film. In food-contact uses, polyethylene films are commonly tested under 21 CFR 177.1520 and EU Regulation (EU) No 10/2011; overall migration, specific migration of additives, and organoleptic transfer are lot-specific. In lamination, the uniform comonomer distribution narrows the melting curve, lowers seal initiation temperature, and broadens hot-tack performance. Hot-tack strength can be evaluated to ASTM F1921; seal strength is evaluated to ASTM F88/F88M. For heavy-duty sacks, puncture resistance is measured to ASTM D5748 and dart impact to ASTM D1709; the class-typical improvement in dart impact permits downgauging by 10–20% in some constructions, provided that tear strength and stiffness remain within specification. Agricultural film longevity is assessed by accelerated weathering to ASTM D4329 or ISO 4892-2, but QHM22F is not supplied with UV stabilizer unless specifically ordered.
Seal response is governed by the melting range rather than density alone. Differential scanning calorimetry to ISO 11357-3:2018 on QHM22F-class resins typically yields a single peak melting temperature of 105–125 °C; the lower molecular-weight tail and uniform branch distribution narrow the melting endotherm. This narrow endotherm reduces the temperature interval between melt initiation and complete flow, which permits lower heat-seal bar settings and higher line speeds on vertical form-fill-seal machines. However, it also reduces the high-temperature plateau in seal strength; seal bar temperature must be controlled within a narrower window than with Ziegler-Natta LLDPE. Hot-tack testing to ASTM F1921 on laminates or coextruded structures is therefore recommended before replacing a conventional C4-LLDPE sealant layer.
The replacement is not a one-to-one drop-in under all conditions. On cast-film and lamination lines equipped with chill-roll casting, the narrow molecular-weight distribution reduces melt curtain stability, and neck-in may increase if the die-to-roll gap is too wide. A die-to-chill-roll gap of 20–40 mm and a melt temperature 5–10 °C higher than that used for Ziegler-Natta LLDPE are common adjustments. On blown-film lines, the lower melt strength may require a higher frost-line position or the addition of 5–15 wt% high-pressure LDPE for deep-gauge or high-blow-up-ratio structures. Compared with Ziegler-Natta C4-LLDPE, QHM22F is expected to show lower seal initiation temperature, improved dart impact, and reduced haze but may exhibit lower machine-direction tear and lower bubble stability. Compared with high-pressure LDPE, QHM22F has lower melt strength and less strain hardening but superior tensile toughness and downgauging potential.
Storage and handling recommendations for QHM22F are those of polyethylene film resins. The pellets are not hygroscopic, but surface condensation should be avoided to prevent moisture feed and bubble defects. In high-humidity environments or when cold pellets are transferred into a warm production hall, a dehumidified-air hopper set at 60–70 °C for 2–4 h reduces surface moisture. Storage at ambient temperature below 50 °C, away from direct sunlight, and in sealed containers maintains additive integrity. Dry-blending with incompatible acid-functional polymers or amine-rich concentrates should be avoided because they may alter organoleptic performance or react with catalyst residues. Reclaimed QHM22F film scrap may be re-extruded in controlled fractions up to 20 wt% in non-food-contact layers if the scrap is clean and has not been subjected to multiple heat histories. Food-contact use of rework remains subject to local regulatory approval and lot-specific compliance documentation.